Lithium extraction with coated ion exchange particles

ABSTRACT

The present invention relates to the extraction of lithium from liquid resources such as natural and synthetic brines, leachate solutions from minerals, and recycled products.

CROSS-REFERENCE

This application claims the benefit of U.S. Provisional Application No.62/421,934, filed Nov. 14, 2016, which application is incorporatedherein by reference.

BACKGROUND OF THE INVENTION

Lithium is an essential element for high-energy rechargeable batteriesand other technologies. Lithium can be found in a variety of liquidsolutions, including natural and synthetic brines, leachate solutionsfrom minerals, and recycled products.

SUMMARY OF THE INVENTION

Lithium can be extracted from liquid resources using an ion exchangeprocess based on inorganic ion exchange materials. Inorganic ionexchange materials absorb lithium ions from a liquid resource whilereleasing hydrogen ions, and then elute lithium ions in acid whileabsorbing hydrogen ions. The ion exchange process can be repeated toextract lithium ions from a liquid resource and yield a concentratedlithium ion solution. The concentrated lithium ion solution can befurther processed into chemicals for the battery industry or otherindustries.

A major challenge for lithium extraction using inorganic ion exchangematerials is the dissolution and degradation of materials. This isespecially so during lithium elution in acid but also during lithiumuptake in liquid resources. To yield a concentrated lithium solutionfrom the ion exchange process, it is desirable to use a concentratedacid solution to elute the lithium. However, concentrated acid solutionsdissolve and degrade inorganic ion exchange materials, which decreasethe performance and lifespan of the materials. There is a need thereforefor a method of extracting lithium ions in which inorganic ion exchangematerials are protected from dissolution and degradation.

An aspect described herein is a coated ion exchange particle comprisingan ion exchange material and a coating material.

In some embodiments, the coating material prevents dissolution of theion exchange material. In some embodiments, the coating material allowsdiffusion of lithium ions and hydrogen ions to and from the ion exchangematerial.

In some embodiments, the coating material comprises a carbide, anitride, an oxide, a phosphate, a fluoride, a polymer, carbon, acarbonaceous material, or combinations thereof. In some embodiments, thecoating material comprises TiO₂, ZrO₂, MoO₂, SnO₂, Nb₂O₅, Ta₂O₅,Li₂TiO₃, SiO₂, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, LiTaO₃, AlPO₄, LaPO₄, ZrSiO₄,ZrP₂O₇, MOP₂O₇, MO₂P₃O₁₂, BaSO₄, AlF₃, SiC, TiC, ZrC, Si₃N₄, ZrN, BN,carbon, graphitic carbon, amorphous carbon, hard carbon, diamond-likecarbon, solid solutions thereof, or combination thereof. In someembodiments, the coating material comprises TiO₂. In some embodiments,the coating material comprises SiO₂. In some embodiments, the coatingmaterial comprises ZrO₂.

In some embodiments, the ion exchange material comprises an oxide, aphosphate, an oxyfluoride, a fluorophosphate, or combinations thereof.In some embodiments, the ion exchange material is selected fromLi₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃, Li₂MnO₃, Li₂SnO₃, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiAlO₂, LiCuO₂, LiTiO₂, Li₄TiO₄, Li₇Ti₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, LiFePO₄, LiMnPO₄, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O,SnO₂.xSb₂O₅.yH₂O, TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, andcombinations thereof. In some embodiment, x is selected from 0.1, 0.2,0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. Insome embodiments, y is selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, x andy is independently selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8,0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, the ionexchange material is selected from Li₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂,Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, and combinations thereof.

In some embodiments, the coated ion exchange particle has an averagediameter of less than 100 μm. In some embodiments, the coated ionexchange particle has an average diameter of less than 10 μm. In someembodiments, the coated ion exchange particle has an average diameter ofless than 1,000 nm. In some embodiments, the coated ion exchangeparticle has an average diameter of less than 100 nm.

An aspect described herein is a porous structure for ion exchangecomprising: a) a structural support; and b) a plurality of particlesselected from coated ion exchange particles, uncoated ion exchangeparticles, and a combination thereof.

In some embodiments, the structural support comprises a polymer, anoxide, a phosphate, or combinations thereof. In some embodiments, thestructural support comprises a polymer. In some embodiments, the polymeris polyvinylidene fluoride, polyvinyl fluoride, polyvinyl chloride,polyvinylidene chloride, a chloro-polymer, a fluoro-polymer, afluoro-chloro-polymer, polyethylene, polypropylene, polyphenylenesulfide, polytetrafluoroethylene, sulfonated polytetrafluoroethylene,polystyrene, polydivinylbenzene, polybutadiene, a sulfonated polymer, acarboxylated polymer, polyacrylonitrile, tetrafluoroethylene,perfluoro-3,6-dioxa-4-ethyl-7-octene-sulfonic acid (NAFION® (copolymerof perfluoro-3,6-dioxa-4-methyl-7octene-sulfonic acid andtetrafluoroethylene)), copolymers thereof, or combinations thereof.

In some embodiments, the porous structure has a connected network ofpores that enables liquid solutions to penetrate quickly into the beadand deliver lithium ion and hydrogen ions to and from ion exchangeparticles in the bead. In some embodiments, the porous structure has aconnected network of pores that are structured to enable fastinfiltration by liquid solutions to create liquid diffusion channelsfrom the bead surface to the ion exchange particles in the bead. In someembodiments, the porous bead has a hierarchical connected network ofpores with a distribution of pore sizes such that the pore networkcreates pathways between the surface of the bead and the ion exchangeparticles in the bead. In some embodiments, the porous structureincludes pores with diameters ranging from less than 10 μm to greaterthan 50 μm. In some embodiments, the porous structure includes poreswith diameters ranging from more than 1 μm, more than 2 μm, more than 4μm, more than 6 μm, more than 8 μm, more than 10 μm, more than 15 μm,more than 20 μm, more than 40 μm, more than 60 μm, more than 80 μm, morethan 100 μm, less than 2 μm, less than 4 μm, less than 6 μm, less than 8μm, less than 10 μm, less than 15 μm, less than 20 μm, less than 40 μm,less than 60 μm, less than 80 μm, less than 100 μm, from about 1 μm toabout 100 μm, from about 5 μm to about 75 μm, or from about 10 μm toabout 50 μm.

In some embodiments, the porous structure forms a porous membrane,porous bead, other porous structure, dense membrane, dense bead,scaffold, a woven membrane, a wound membrane, a spiral wound membrane,or combinations thereof. In some embodiments, the porous structure formsa porous membrane, a porous bead, or combinations thereof.

In some embodiments, the coated ion exchange particles comprise an ionexchange material and a coating material. In some embodiments, thecoating material of the coated ion exchange particles preventsdissolution of the ion exchange material. In some embodiments, thecoating material of the coated ion exchange particles allows diffusionof lithium ions and hydrogen ions to and from the ion exchange material.

In some embodiments, the coating material of the coated ion exchangeparticles comprises a carbide, a nitride, an oxide, a phosphate, afluoride, a polymer, carbon, a carbonaceous material, or combinationsthereof. In some embodiments, the coating material of the coated ionexchange particles comprises TiO₂, ZrO₂, MoO₂, SnO₂, Nb₂O₅, Ta₂O₅,Li₂TiO₃, SiO₂, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, LiTaO₃, AlPO₄, LaPO₄, ZrSiO₄,ZrP₂O₇, MoP₂O₇, Mo₂P₃O₁₂, BaSO₄, AlF₃, SiC, TiC, ZrC, Si₃N₄, ZrN, BN,carbon, graphitic carbon, amorphous carbon, hard carbon, diamond-likecarbon, solid solutions thereof, or combination thereof. In someembodiments, the coating material of the coated ion exchange particlescomprises TiO₂. In some embodiments, the coating material of the coatedion exchange particles comprises SiO₂. In some embodiments, the coatingmaterial of the coated ion exchange particles comprises ZrO₂.

In some embodiments, the ion exchange material of the coated ionexchange particle comprises an oxide, a phosphate, an oxyfluoride, afluorophosphate, or combinations thereof. In some embodiments, the ionexchange material of the coated ion exchange particle is selected fromLi₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃, Li₂MnO₃, Li₂SnO₃, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiAlO₂, LiCuO₂, LiTiO₂, Li₄TiP₄, Li₇Ti₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, LiFePO₄, LiMnPO₄, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O,SnO₂.xSb₂O₅.yH₂O, TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, andcombinations thereof. In some embodiment, x is selected from 0.1, 0.2,0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. Insome embodiments, y is selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, x andy is independently selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8,0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, or 10. In some embodiments, the ionexchange material of the coated ion exchange particle is selected fromLi₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂, Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, andcombinations thereof.

In some embodiments, the coated ion exchange particle has an averagediameter of less than 100 μm. In some embodiments, the coated ionexchange particle has an average diameter of less than 10 μm. In someembodiments, the coated ion exchange particle has an average diameter ofless than 1,000 nm. In some embodiments, the coated ion exchangeparticle has an average diameter of less than 100 nm.

In some embodiments, the uncoated ion exchange particles comprise an ionexchange material. In some embodiments, the ion exchange material of theuncoated ion exchange particle comprises an oxide, a phosphate, anoxyfluoride, a fluorophosphate, or combinations thereof. In someembodiments, the ion exchange material of the uncoated ion exchangeparticle is selected Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃, Li₂MnO₃, Li₂SnO₃,LiMn₂O₄, Li_(1.6)Mn_(1.6)O₄, LiAlO₂, LiCuO₂, LiTiO₂, Li₄TiO₄,Li₇Ti₁₁O₂₄, Li₃VO₄, Li₂Si₃O₇, LiFePO₄, LiMnPO₄, Li₂CuP₂O₇, Al(OH)₃,LiCl.xAl(OH)₃.yH₂O, SnO₂.xSb₂O₅.yH₂O, TiO₂.xSb₂O₅.yH₂O, solid solutionsthereof, and combinations thereof. In some embodiment, x is selectedfrom 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7,8, 9, and 10. In some embodiments, y is selected from 0.1, 0.2, 0.3,0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In someembodiments, x and y is independently selected from 0.1, 0.2, 0.3, 0.4,0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In someembodiments, the ion exchange material of the uncoated ion exchangeparticle is selected from Li₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂,Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, and combinations thereof.

In some embodiments, the uncoated ion exchange particle has an averagediameter of less than 100 μm. In some embodiments, the uncoated ionexchange particle has an average diameter of less than 10 μm. In someembodiments, the uncoated ion exchange particle has an average diameterof less than 1,000 nm. In some embodiments, the uncoated ion exchangeparticle has an average diameter of less than 100 nm.

In some embodiments, the porous structure is in the form of a porousbead. In some embodiments, the porous bead is approximately spherical.In some embodiments, the porous bead has an average diameter of lessthan 10 cm. In some embodiments, the porous bead has an average diameterof less than 1 cm. In some embodiments, the porous bead has an averagediameter of less than 1 mm. In some embodiments, the porous bead had anaverage diameter of less than 100 μm. In some embodiments, the porousbead has an average diameter of less than 10 μm. In some embodiments,the porous bead is approximately spherical with an average diameter offrom about 1 μm to about 100 μm, from about 1 mm to about 100 mm, fromabout 1 mm to about 80 mm, from about 1 mm to about 60 mm, from about 1to about 40 mm, from about 1 to about 20 mm, from about 1 to about 10mm, from about 1 cm to about 10 cm, from about 1 cm to about 8 cm, fromabout 1 cm to about 6 cm, or from about 1 cm to about 4 cm.

In some embodiments, the porous bead is tablet-shaped. In someembodiments, the porous bead has a diameter of less than 20 mm and aheight of less than 20 mm. In some embodiments, the porous bead has adiameter of less than 8 mm and a height of less than 8 mm. In someembodiments, the porous bead has a diameter of less than 4 mm and aheight of less than 4 mm. In some embodiments, the porous bead has adiameter of less than 2 mm and a height of less than 2 mm. In someembodiments, the porous bead has a diameter of less than 1 mm and aheight of less than 1 mm.

An aspect described herein is a method of extracting lithium from aliquid resource, comprising: contacting the coated ion exchange particlewith a liquid resource to produce lithiated coated ion exchangeparticles; and treating the lithiated coated ion exchange particles withan acid solution to produce a salt solution comprising lithium ions. Insome embodiments, the liquid resource is a natural brine, a dissolvedsalt flat, seawater, concentrated seawater, a desalination effluent, aconcentrated brine, a processed brine, an oilfield brine, a liquid froman ion exchange process, a liquid from a solvent extraction process, asynthetic brine, a leachate from an ore or combination of ores, aleachate from a mineral or combination of minerals, a leachate from aclay or combination of clays, a leachate from recycled products, aleachate from recycled materials, or combinations thereof. In someembodiments, the acid solution comprises hydrochloric acid, sulfuricacid, phosphoric acid, hydrobromic acid, chloric acid, perchloric acid,nitric acid, formic acid, acetic acid, or combinations thereof. In someembodiments, the salt solution further comprises an impurity derivedfrom the coated ion exchange particle. In some embodiments, the impurityis present in a concentration of more than 1 ppb, more than 5 ppb, morethan 10 ppb, more than 100 ppb, more than 1 ppm, more than 2 ppm, morethan 4 ppm, more than 6 ppm, more than 8 ppm, less than 10 ppm, lessthan 8 ppm, less than 6 ppm, less than 4 ppm, less than 2 ppm, less than1 ppm, less than 100 ppb, less than 10 ppb, less than 5 ppb, from about1 ppb to about 10 ppm, from about 5 ppb to about 10 ppm, from about 10ppb to about 10 ppm, from about 50 ppb to about 10 ppm, from about 100ppb to about 10 ppm, from about 1 ppm to about 10 ppm, from about 2 ppmto about 10 ppm, from about 4 ppm to about 10 ppm, from about 6 ppm toabout ppm, or from about 8 ppm to about 10 ppm.

An aspect described herein is a method of extracting lithium from aliquid resource, comprising: contacting the porous structure with aliquid resource to produce a lithiated porous structure; and treatingthe lithiated porous structure with an acid solution to produce a saltsolution comprising lithium ions. In some embodiments, the liquidresource is a natural brine, a dissolved salt flat, seawater,concentrated seawater, a desalination effluent, a concentrated brine, aprocessed brine, an oilfield brine, a liquid from an ion exchangeprocess, a liquid from a solvent extraction process, a synthetic brine,a leachate from an ore or combination of ores, a leachate from a mineralor combination of minerals, a leachate from a clay or combination ofclays, a leachate from recycled products, a leachate from recycledmaterials, or combinations thereof. In some embodiments, the acidsolution comprises hydrochloric acid, sulfuric acid, phosphoric acid,hydrobromic acid, chloric acid, perchloric acid, nitric acid, formicacid, acetic acid, or combinations thereof.

An aspect described herein is a method of extracting lithium from aliquid resource, comprising: contacting the porous bead with a liquidresource to produce lithiated porous beads; and treating the lithiatedporous beads with an acid solution to produce a salt solution comprisinglithium ions. In some embodiments, the liquid resource is a naturalbrine, a dissolved salt flat, seawater, concentrated seawater, adesalination effluent, a concentrated brine, a processed brine, anoilfield brine, a liquid from an ion exchange process, a liquid from asolvent extraction process, a synthetic brine, a leachate from an ore orcombination of ores, a leachate from a mineral or combination ofminerals, a leachate from a clay or combination of clays, a leachatefrom recycled products, a leachate from recycled materials, orcombinations thereof. In some embodiments, the acid solution compriseshydrochloric acid, sulfuric acid, phosphoric acid, hydrobromic acid,chloric acid, perchloric acid, nitric acid, formic acid, acetic acid, orcombinations thereof.

In some embodiments, the method is conducted in a column.

INCORPORATION BY REFERENCE

All publications, patents, and patent applications mentioned in thisspecification are herein incorporated by reference to the same extent asif each individual publication, patent, or patent application wasspecifically and individually indicated to be incorporated by reference.

BRIEF DESCRIPTION OF THE DRAWINGS

The novel features of the invention are set forth with particularity inthe appended claims. A better understanding of the features andadvantages of the present invention will be obtained by reference to thefollowing detailed description that sets forth illustrative embodiments,in which the principles of the invention are utilized, and theaccompanying drawings of which:

FIG. 1 depicts the coated ion exchange particle with ion exchangematerial 1 and a coating material 2 protecting the coated ion exchangeparticle surface.

FIG. 2 depicts a porous polymer bead 3 supporting coated ion exchangeparticle(s) 4.

FIG. 3 depicts an ion exchange column 5 loaded with porous polymer beads3 supporting coated ion exchange particle(s).

FIG. 4 demonstrates decreased dissolution during acid treatment forcoated ion exchange particles relative to uncoated ion exchangeparticles.

DETAILED DESCRIPTION OF THE INVENTION

The terms “lithium”, “lithium ion”, and “Li⁺” are used interchangeablyin the present specification and these terms are synonymous unlessspecifically noted to the contrary. The terms “hydrogen”, “hydrogenion”, “proton”, and “H⁺” are used interchangeably in the presentspecification and these terms are synonymous unless specifically notedto the contrary.

Coated Ion Exchange Particle

In an aspect described herein are coated ion exchange particlescomprising ion exchange material and coating material.

Coating Material of Coated Ion Exchange Particle

In some embodiments, the coating material prevents the dissolution ofthe ion exchange material. In some embodiments, the coating materialprotects the ion exchange material from dissolution and degradationduring lithium elution in acid, during lithium uptake from a liquidresource, and during other embodiments of an ion exchange process. Insome embodiments, the coating material enables the use of concentratedacids in the ion exchange process to: (1) yield concentrated lithium ionsolutions; (2) shift the equilibrium such that lithium ions move fromthe ion exchange material; and (3) maximize ion exchange capacity of theion exchange material. One example of a coated ion exchange particle isshown in FIG. 1.

In some embodiments, the coating material allows diffusion to and fromthe ion exchange material. In particular, the coating materialfacilitates diffusion of lithium ions and hydrogen ions between thecoated ion exchange particles and various liquid resources. In someembodiments, the coating material enables the adherence of coated ionexchange particles to a structural support and suppresses structural andmechanical degradation of the coated ion exchange particles.

In some embodiments, the coating material comprises a carbide, anitride, an oxide, a phosphate, a fluoride, a polymer, carbon, acarbonaceous material, or combinations thereof. In some embodiments, thecoating material comprises Nb₂O₅, Ta₂O₅, MoO₂, TiO₂, ZrO₂, MoO₂, SnO₂,SiO₂, Li₂O, Li₂TiO₃, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, LiTaO₃, Li₂SiO₃,Li₂Si₂O₅, Li₂MnO₃, ZrSiO₄, AlPO₄, LaPO₄, ZrP₂O₇, MoP₂O₇, Mo₂P₃O₁₂,BaSO₄, AlF₃, SiC, TiC, ZrC, Si₃N₄, ZrN, BN, carbon, graphitic carbon,amorphous carbon, hard carbon, diamond-like carbon, solid solutionsthereof, or combinations thereof. In some embodiments, the coatingmaterial comprises polyvinylidene difluoride, polyvinyl chloride, afluoro-polymer, a chloro-polymer, or a fluoro-chloro-polymer. In someembodiments, the coating material comprises TiO₂, ZrO₂, SiO₂ MoO₂,Li₂TiO₃, Li₂ZrO₃, Li₂MnO₃, ZrSiO₄, or LiNbO₃, AlF₃, SiC, Si₃N₄,graphitic carbon, amorphous carbon, diamond-like carbon, or combinationsthereof. In some embodiments, the coating material comprises TiO₂, SiO₂,or ZrO₂. In some embodiments, the coating material comprises TiO₂. Insome embodiments, the coating material comprises SiO₂. In someembodiments, the coating material comprises ZrO₂.

In some embodiments, the coating coats primary ion exchange particles orsecondary ion exchange particles. In some embodiments, the coating coatsboth the primary ion exchange particles and the secondary ion exchangeparticles. In some embodiments, the primary ion exchange particles havea first coating and the secondary ion exchange particles have a secondcoating that is identical, similar, or different in composition to thefirst coating.

In some embodiments, the coating material has a thickness of less than 1nm, less than 10 nm, less than 100 nm, less than 1,000 nm, less than10,000 nm, more than 1 nm, more than 10 nm, more than 100 nm, more than1,000 nm, more than 10,000 nm, from about 1 nm to about 10,000 nm, fromabout 10 nm, to about 1,000 nm, or from about 100 to about 1,000 nm. Insome embodiments, the coating material has a thickness of less than 5nm, less than 10 nm, less than 50 nm, less than 100 nm, less than 500nm, more than 1 nm, more than 5 nm, more than 10 nm, more than 50 nm,more than 100 nm, from about 1 nm to about 500 nm, from about 1 nm toabout 100 nm, from about 1 nm to about 50 nm, from about 1 nm to about10 nm, from about 1 nm to about 5 nm, or from about 5 nm to about 100nm.

In some embodiments, the coating material is deposited by a method suchas chemical vapor deposition, atomic layer deposition, physical vapordeposition, hydrothermal, solvothermal, sol-gel, solid state, moltensalt flux, ion exchange, microwave, chemical precipitation,co-precipitation, ball milling, pyrolysis, or combinations thereof. Insome embodiments, the coating material is deposited by a method such aschemical vapor deposition, hydrothermal, solvothermal, sol-gel,precipitation, microwave sol-gel, chemical precipitation, orcombinations thereof. In some embodiments, the coating materials isdeposited in a reactor that is a batch tank reactor, a continuous tankreactor, a batch furnace, a continuous furnace, a tube furnace, a rotarytube furnace, or combinations thereof.

In some embodiments, the coating material is deposited in a reactor bysuspending the ion exchange material in a solvent with reagents that isadded all at once or added over time. In some embodiments, the reagentsare added in a specific time series to control reaction rates andcoating depositions. In some embodiments, the solvent is aqueous ornon-aqueous. In some embodiments, the solvent is an alcohol such asethanol, propanol, butanol, pentanol, hexanol, septanol, or octanol. Insome embodiments, the reagents include metal chlorides, metal oxides,metal alkoxides, metal oxychlorides, metalloid oxides, metalloidalkoxides, metalloid chlorides, metalloid oxychlorides, or combinationsthereof. In some embodiments, the reagents include monomers, oligomers,polymers, gels, or combinations thereof. In some embodiments, thereagents include water, oxidants, reductants, acids, bases, orcombinations thereof. In some embodiments, the reagents are added in thepresence of catalysts such as acids, bases, or combinations thereof. Insome embodiments, the reagents are added during a time period of lessthan 1 minute, less than 1 hour, less than 1 day, less about 1 week,more than 1 minute, more than 1 hour, more than 1 day, from about 1minute to about 60 minutes, from about 1 hour to about 24 hours, or fromabout 1 day to about 7 days. In some embodiments, the reagents aredripped into the reactor continuously or at intervals. In someembodiments, multiple reagents are added to the reactor at differentrates. In some embodiments, some reagents are combined separately andreacted to form a gel or polymer prior to addition to the reactor.

In some embodiments, the freshly coated ion exchange material is heatedto one or more temperatures to age, dry, react, or crystallize thecoating. In some embodiments, the freshly coated ion exchange materialis heated to a temperature of less than about 100° C., less than about200° C., less than about 300° C., less than about 400° C., less thanabout 500° C., less than about 600° C., less than about 700° C., or lessthan about 800° C. In some embodiments, the freshly coated ion exchangematerial is heated to a temperature of more than about 100° C., morethan about 200° C., more than about 300° C., more than about 400° C.,more than about 500° C., more than about 600° C., more than about 700°C., or more than about 800° C. In some embodiments, the freshly coatedion exchange material is heated to a temperature from about 100° C. toabout 800° C., from about 200° C. to about 800° C., from about 300° C.to about 700° C., from about 400° C. to about 700° C., from about 500°C. to about 700° C., from about 100° C. to about 300° C., from about200° C. to about 400° C., from about 300° C. to about 500° C., fromabout 400° C. to about 600° C., from about 500° C. to about 700° C., orfrom about 600° C. to about 800° C. In some embodiments, the freshlycoated ion exchange material is heated in an atmosphere of aircomprising oxygen, nitrogen, hydrogen, argon, or combinations thereof.In some embodiments, the freshly coated ion exchange material is heatedfor a time period of less than about 1 hour, less than about 2 hours,less than about 4 hours, less than about 8 hours, less than about 24hours, more than 1 hour, more than 2 hours, more than 4 hours, more than8 hours, from about 0.5 hours to about 24 hours, from about 0.5 hours toabout 8 hours, from about 0.5 hours to about 4 hours, from about 0.5hours to about 2 hours, or from about 0.5 hours to about 1 hour.

In some embodiments, the coating material is deposited with physicalcharacteristics such as crystalline, amorphous, full coverage, partialcoverage, uniform, non-uniform, or combinations thereof. In someembodiments, multiple coatings are deposited on the ion exchangematerial in an arrangement such as concentric, patchwork, orcombinations thereof.

Ion Exchange Material of Coated Ion Exchange Particle

In some embodiments, the ion exchange material is suitable for highlithium absorption capacity and for lithium ions in a liquid resourcerelative to other ions such as sodium ions and magnesium ions. In someembodiments, the ion exchange material is suitable for strong lithiumion uptake in liquid resources including those with low concentrationsof lithium ions, facile elution of lithium ions with a small excess ofacid, and fast ionic diffusion.

In some embodiments, the ion exchange material comprises an oxide, aphosphate, an oxyfluoride, a fluorophosphate, or combinations thereof.In a further embodiment, the ion exchange material comprises LiFePO₄,LiMnPO₄, Li₂MO₃ (M=Ti, Mn, Sn), Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiMO₂ (M=Al, Cu, Ti), Li₄TiO₄, Li₇T₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O, SnO₂.xSb₂O₅.yH₂O,TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, or combinations thereof. Insome embodiment, x is selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, y isselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, x and y is independentlyselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, an ion exchange materialcomprises LiFePO₄, Li₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂, Li₄Mn₅O₁₂,Li_(1.6)Mn_(1.6)O₄, solid solutions thereof, or combinations thereof.

In some embodiments, the ion exchange material is synthesized by amethod such as hydrothermal, solvothermal, sol-gel, solid state, moltensalt flux, ion exchange, microwave, ball milling, chemicalprecipitation, co-precipitation, vapor deposition, or combinationsthereof. In some embodiments, the ion exchange material is synthesizedby a method such as chemical precipitation, hydrothermal, solid state,microwave, or combinations thereof.

In some embodiments, the ion exchange materials are synthesized in alithiated state with a sub-lattice fully or partly occupied by lithiumions. In some embodiments, the ion exchange materials are synthesized ina hydrated state with a sub-lattice fully or partly occupied by hydrogenions.

In some embodiments, the ion exchange material and the coating materialform one or more concentration gradients where the chemical compositionof the coated ion exchange particle varies between two or morecompositions. In some embodiments, the chemical composition variesbetween the ion exchange materials and the coating in a manner that iscontinuous, discontinuous, or continuous and discontinuous in differentregions of the coated ion exchange particle. In some embodiments, theion exchange materials and the coating materials form a concentrationgradient that extends over a thickness of less than 1 nm, less than 10nm, less than 100 nm, less than 1,000 nm, less than 10,000 nm, less than100,000 nm, more than 1 nm, more than 10 nm, more than 100 nm, more than1,000 nm, more than 10,000 nm, from about 1 nm to about 100,000 nm, fromabout 10 nm to about 10,000 nm, or from about 100 to about 1,000 nm.

Particle Size of Coated Ion Exchange Particle

In some embodiments, the coated ion exchange particle has an averagediameter of less than about 10 nm, less than about 20 nm, less thanabout 30 nm, less than about 40 nm, less than about 50 nm, less thanabout 60 nm, less than about 70 nm, less than about 80 nm, less thanabout 90 nm, less than about 100 nm, less than about 1,000 nm, less thanabout 10,000 nm, less than about 100,000 nm, more than about 10 nm, morethan about 20 nm, more than about 30 nm, more than about 40 nm, morethan about 50 nm, more than about 60 nm, more than about 70 nm, morethan about 80 nm, more than about 90 nm, more than about 100 nm, morethan about 1,000 nm, more than about 10,000 nm, from about 1 nm to about10,000 nm, from about 1 nm to about 1,000 nm, from about 1 nm to about100 nm, from about 1 nm to about 80 nm, from about 1 nm to about 60 nm,from about 1 nm to about 40 nm, or from about 1 nm to about 20 nm. Insome embodiments, the coated ion exchange particles have an average sizeof less than about 100 nm, less than about 1,000 nm, or less than about10,000 nm. In some embodiments, the coated ion exchange particles aresecondary particles comprised of smaller primary particles, wherein thesecondary particles have an average diameter of less than about 10 nm,less than about 20 nm, less than about 30 nm, less than about 40 nm,less than about 50 nm, less than about 60 nm, less than about 70 nm,less than about 80 nm, less than about 90 nm, less than about 100 nm,less than about 1,000 nm, less than about 10,000 nm, less than about100,000 nm, more than about 10 nm, more than about 20 nm, more thanabout 30 nm, more than about 40 nm, more than about 50 nm, more thanabout 60 nm, more than about 70 nm, more than about 80 nm, more thanabout 90 nm, more than about 100 nm, more than about 1,000 nm, more thanabout 10,000 nm, from about 1 nm to about 10,000 nm, from about 1 nm toabout 1,000 nm, from about 1 nm to about 100 nm, from about 1 nm toabout 80 nm, from about 1 nm to about 60 nm, from about 1 nm to about 40nm, or from about 1 nm to about 20 nm.

In some embodiments, the coated ion exchange particle has an averagediameter of less than about 10 μm, less than about 20 μm, less thanabout 30 μm, less than about 40 μm, less than about 50 μm, less thanabout 60 μm, less than about 70 μm, less than about 80 μm, less thanabout 90 μm, less than about 100 μm, less than about 1,000 μm, less thanabout 10,000 μm, less than about 100,000 μm, more than about 10 μm, morethan about 20 μm, more than about 30 μm, more than about 40 μm, morethan about 50 μm, more than about 60 μm, more than about 70 μm, morethan about 80 μm, more than about 90 μm, more than about 100 μm, morethan about 1,000 μm, more than about 10,000 μm, from about 1 μm to about10,000 μm, from about 1 μm to about 1,000 μm, from about 1 μm to about100 μm, from about 1 μm to about 80 μm, from about 1 μm to about 60 μm,from about 1 μm to about 40 μm, or from about 1 μm to about 20 μm. Insome embodiments, the coated ion exchange particles have an average sizeof less than about 100 μm, less than about 1,000 μm, or less than about10,000 μm. In some embodiments, the coated ion exchange particles aresecondary particles comprised of smaller primary particles, wherein thesecondary particles have an average diameter of less than about 10 μm,less than about 20 μm, less than about 30 μm, less than about 40 μm,less than about 50 μm, less than about 60 μm, less than about 70 μm,less than about 80 μm, less than about 90 μm, less than about 100 μm,less than about 1,000 μm, less than about 10,000 μm, less than about100,000 μm, more than about 10 μm, more than about 20 μm, more thanabout 30 μm, more than about 40 μm, more than about 50 μm, more thanabout 60 μm, more than about 70 μm, more than about 80 μm, more thanabout 90 μm, more than about 100 μm, more than about 1,000 μm, more thanabout 10,000 μm, from about 1 μm to about 10,000 μm, from about 1 μm toabout 1,000 μm, from about 1 μm to about 100 μm, from about 1 μm toabout 80 μm, from about 1 μm to about 60 μm, from about 1 μm to about 40μm, or from about 1 μm to about 20 μm.

In an embodiment, the average diameter of the coated ion exchangeparticles or the average diameter of coated ion exchange particles whichare secondary particles comprised of smaller primary particles, isdetermined by measuring the particle size distribution of the coated ionexchange particles or the coated ion exchange particles which aresecondary particles comprised of smaller primary particles, anddetermining the mean particle size.

In some embodiments, coated ion exchange particles comprise coating onprimary ion exchange particles or secondary ion exchange particles. Insome embodiments, coated ion exchange particles comprise the coating onprimary ion exchange particles and secondary ion exchange particles. Insome embodiments, the secondary ion exchange particles comprise primaryion exchange particles. In some embodiments, the coating is on theprimary ion exchange particles which are a component of the secondaryion exchange particles and a further coating is applied on the secondaryion exchange particles. In some embodiments, the primary ion exchangeparticles have a first coating and the secondary ion exchange particleshave a second coating that is identical, similar, or different incomposition to the first coating.

Porous Structure

In an aspect described herein, coated ion exchange particles, uncoatedion exchange particles, and combinations thereof are optionally embeddedin, adhered to, or otherwise supported by a structural support.

Structural Supports of Porous Structure

In some embodiments, the structural support comprises a polymer, anoxide, a phosphate, or combinations thereof. In some embodiments, thestructural support comprises polyvinylidene difluoride, polyvinylchloride, polyvinyl dichloride, a chloro-polymer, a fluoro-polymer, afluorochloro-polymer, polyethylene, polypropylene, polyphenylenesulfide, polytetrafluoroethylene, polytetrofluoroethylene, sulfonatedpolytetrofluoroethylene, polystyrene, polydivinylbenzene, polybutadiene,sulfonated polymer, carboxylated polymer, polyacrylonitrile,polyacrylonitrile, tetrafluoroethylene,perfluoro-3,6-dioxa-4-methyl-7-octene-sulfonic acid (NAFION® (copolymerof perfluoro-3,6-dioxa-4-methyl-7octene-sulfonic acid andtetrafluoroethylene)), copolymers thereof, and combinations thereof. Insome embodiments, a structural support is selected from: polyvinylidenedifluoride, polyvinyl chloride, sulfonated polytetrofluoroethylene,polystyrene, polydivinylbenzene, copolymers thereof, or combinationsthereof. In some embodiments, a structural support is selected from:titanium dioxide, zirconium dioxide, silicon dioxide, solid solutionsthereof, or combinations thereof. In some embodiments, the structuralsupport is selected for thermal resistance, acid resistance, and/orother chemical resistance.

In some embodiments, the structural support is used with the coated ionexchange particles, uncoated ion exchange particles, and combinationsthereof in a mass ratio of polymer to particles that is about 1:100,about 1:20, about 1:5, about 1:1, about 5:1, about 20:1, from 1:100 toabout 20:1, from 1:20 to 20:1, from 1:5 to 20:1, from 1:1 to 20:1, from5:1 to 20:1, from 1:1 to 1:20, from 1:1 to 1:15, or from 1:1 to 1:10.

In some embodiments, the structural support is a polymer that isdissolved and mixed with the coated ion exchange particles, the uncoatedion exchange particles and combinations thereof, using a solventselected from N-methyl-2-pyrrolidone, dimethyl sulfoxide,tetrahydrofuran, dimethylformamide, dimethylacetamide, methyl ethylketone, and combinations thereof.

Shape of Pores in Porous Structure

In some embodiments, the porous structure has a connected network ofpores that enable liquid solutions to penetrate quickly into the porousstructure and deliver lithium ion and hydrogen ions to and from thecoated ion exchange particles, uncoated ion exchange particles, andcombinations thereof. In some embodiments, the porous structure has aconnected network of pores that are structured to enable fastinfiltration by liquid solutions to create liquid diffusion channelsfrom the porous structure surface to the coated ion exchange particles,uncoated ion exchange particles, and combinations thereof.

In some embodiments, the porous structure has a hierarchical connectednetwork of pores with a distribution of pore sizes such that the porenetwork creates pathways between the surface of the porous structure andthe coated ion exchange particles, uncoated ion exchange particles, andcombinations thereof in the porous structure. In some embodiments, thehierarchical connected network of pores comprises large channels fromwhich medium channels branch from and/or medium channels from whichsmall channels branch from. In some embodiments, the hierarchicalconnected network of pores comprises small channels converging to mediumchannels and/or medium channels converging to large channels. In someembodiments, the hierarchical connected network of pores creates fastpenetration of liquid solutions into the pores. In some embodiments, thehierarchical connected network of pores creates fast diffusion oflithium ions and protons through the pores from the surface of theporous structure to the coated ion exchange particles, uncoated ionexchange particles, and combinations thereof in the porous structure.

Size of Pores in Porous Structure

In some embodiments, the porous structure includes pores with diametersranging from less than 10 μm to greater than 50 μm. In some embodiments,the porous structure includes pores with diameters of less than about 1μm, less than about 2 μm, less than about 3 μm, less than about 4 μm,less than about 5 μm, less than about 6 μm, less than about 7 μm, lessthan about 8 μm, less than about 9 μm, less than about 10 μm, less thanabout 20 μm, less than about 30 μm, or less than about 40 μm. In someembodiments, the porous structure includes pores with diameters of morethan about 10 μm, more than about 20 μm, more than about 30 μm, morethan about 40 μm, more than about 50 μm, more than about 60 μm, morethan about 70 μm, more than about 80 μm, more than about 90 μm, or morethan about 100 μm. In some embodiments, the porous structure includespores with diameters from about 1 μm to about 100 μm, from about 5 μm toabout 90 μm, from about 10 μm to about 80 μm, from about 20 μm to about70 μm, or from about 30 μm to about 60 μm.

Forms of Porous Structures

In some embodiments, coated ion exchange particles, uncoated ionexchange particles, and combinations thereof are embedded in a supportstructure, which is a membrane, a spiral-wound membrane, a hollow fibermembrane, or a mesh. In some embodiments, the coated ion exchangeparticles, uncoated ion exchange particles, and combinations thereof areembedded on a support structure comprised of a polymer, a ceramic, orcombinations thereof. In some embodiments, the porous structure isloaded directly into a column with no additional support structure.

In some embodiments, the structural support takes the form of a porousmembrane, porous bead, other porous structure, dense membrane, densebead, scaffold, or combinations thereof. In some embodiments, thestructural support takes the form of a porous membrane, porous bead, orcombinations thereof. One example of a structural support is a porousbead, shown in FIG. 2.

In some embodiments, the structural support is a bead with an averagediameter less than about 10 μm, less than about 100 μm, less than about1 mm, less than about 1 cm, or less than about 10 cm, more than morethan 10 μm, more than 100 μm, more than 1 mm, more than 1 cm, from about1 μm to about 10 cm, from about 10 μm to about 1 cm, from about 100 μmto about 1 cm, from about 1 mm to about 1 cm, from about 0.5 mm to about1 cm, from about 0.25 mm to about 1 cm, from about 0.25 mm to about 100mm, from about 0.25 mm to about 75 mm, from about 0.25 mm to about 50mm, from about 0.25 mm to about 25 mm, from about 0.25 mm to about 10mm, or from about 10 mm to about 1 cm. In some embodiments, thestructural support is a bead with an average diameter less than about100 μm, less than about 1 mm, less than 1 cm, less than 2 cm, less than3 cm, less than 4 cm, less than 5 cm, less than 6 cm, less than 7 cm,less than 8 cm, less than 9 cm, or less than about 10 cm. In someembodiments, the structural support is a membrane with an averagethickness less than about 10 μm, less than about 100 μm, less than about1 cm, less than about 10 cm, more than 1 μm, more than 10 μm, more than100 μm, more than 1 cm, from about 1 μm to about 100 μm, or from about 1cm to about 10 cm.

Coated Ion Exchange Particles in Porous Structure

In some embodiments are coated ion exchange particles which are acomponent of a porous structure, wherein the coated ion exchangeparticles comprise ion exchange material and coating material.

Coating Material of Coated on Exchange Particles in Porous Structure

In some embodiments, the coating material prevents the dissolution ofthe ion exchange material. In some embodiments, the coating materialprotects the ion exchange material from dissolution and degradationduring lithium elution in acid, during lithium uptake from a liquidresource, and during other embodiments of an ion exchange process. Insome embodiments, the coating material enables the use of concentratedacids in the ion exchange process to: (1) yield concentrated lithium ionsolutions; (2) shift the equilibrium such that lithium ions move fromthe ion exchange material; and (3) maximize ion exchange capacity of theion exchange material.

In some embodiments, the coating material allows diffusion to and fromthe ion exchange material. In some embodiments, the coating materialfacilitates diffusion of lithium ions and hydrogen ions between thecoated ion exchange particles and various liquid resources. In someembodiments, the coating material enables the adherence of coated ionexchange particles to the structural support and suppresses structuraland mechanical degradation of the coated ion exchange particles.

In some embodiments, the coating material comprises a carbide, anitride, an oxide, a phosphate, a fluoride, a polymer, carbon, acarbonaceous material, or combinations thereof. In some embodiments, thecoating material comprises Nb₂O₅, Ta₂O₅, MoO₂, TiO₂, ZrO₂, MoO₂, SnO₂,SiO₂, Li₂O, Li₂TiO₃, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, LiTaO₃, Li₂SiO₃,Li₂Si₂O₅, Li₂MnO₃, ZrSiO₄, AlPO₄, LaPO₄, ZrP₂O₇, MoP₂O₇, Mo₂P₃O₁₂,BaSO₄, AlF₃, SiC, TiC, ZrC, Si₃N₄, ZrN, BN, carbon, graphitic carbon,amorphous carbon, hard carbon, diamond-like carbon, solid solutionsthereof, or combinations thereof. In some embodiments, the coatingmaterial comprises polyvinylidene difluoride, polyvinyl chloride, afluoro-polymer, a chloro-polymer, or a fluoro-chloro-polymer. In someembodiments, the coating material comprises TiO₂, ZrO₂, SiO₂ MoO₂,Li₂TiO₃, Li₂ZrO₃, Li₂MnO₃, ZrSiO₄, or LiNbO₃, AlF₃, SiC, Si₃N₄,graphitic carbon, amorphous carbon, diamond-like carbon, or combinationsthereof. In some embodiments, the coating material comprises TiO₂, SiO₂,or ZrO₂. In some embodiments, the coating material comprises TiO₂. Insome embodiments, the coating material comprises SiO₂. In someembodiments, the coating material comprises ZrO₂.

In some embodiments, the coating coats primary ion exchange particles orsecondary ion exchange particles. In some embodiments, the coating coatsboth the primary ion exchange particles and the secondary ion exchangeparticles. In some embodiments, the primary ion exchange particles havea first coating and the secondary ion exchange particles have a secondcoating that is identical, similar, or different in composition to thefirst coating.

In some embodiments, the coating material has a thickness of less than 1nm, less than 10 nm, less than 100 nm, less than 1,000 nm, less than10,000 nm, more than 1 nm, more than 10 nm, more than 100 nm, more than1,000 nm, more than 10,000 nm, from about 1 nm to about 10,000 nm, fromabout 10 nm, to about 1,000 nm, or from about 100 to about 1,000 nm. Insome embodiments, the coating material has a thickness of less than 5nm, less than 10 nm, less than 50 nm, less than 100 nm, less than 500nm, more than 1 nm, more than 5 nm, more than 10 nm, more than 50 nm,more than 100 nm, from about 1 nm to about 500 nm, from about 1 nm toabout 100 nm, from about 1 nm to about 50 nm, from about 1 nm to about10 nm, from about 1 nm to about 5 nm, or from about 5 nm to about 100nm.

In some embodiments, the coating material is deposited by a method suchas chemical vapor deposition, atomic layer deposition, physical vapordeposition, hydrothermal, solvothermal, sol-gel, solid state, moltensalt flux, ion exchange, microwave, chemical precipitation,co-precipitation, ball milling, pyrolysis, or combinations thereof. Insome embodiments, the coating material is deposited by a method such aschemical vapor deposition, hydrothermal, solvothermal, sol-gel,precipitation, microwave sol-gel, chemical precipitation, orcombinations thereof. In some embodiments, the coating materials aredeposited in a reactor that is a batch tank reactor, a continuous tankreactor, a batch furnace, a continuous furnace, a tube furnace, a rotarytube furnace, or combinations thereof.

In some embodiments, the coating material is deposited in a reactor bysuspending the ion exchange material in a solvent with reagents that isadded all at once or added over time. In some embodiments, the reagentsare added in a specific time series to control reaction rates andcoating depositions. In some embodiments, the solvent is aqueous ornon-aqueous. In some embodiments, the solvent is an alcohol such asethanol, propanol, butanol, pentanol, hexanol, septanol, or octanol. Insome embodiments, the reagents include metal chlorides, metal oxides,metal alkoxides, metal oxychlorides, metalloid oxides, metalloidalkoxides, metalloid chlorides, metalloid oxychlorides, or combinationsthereof. In some embodiments, the reagents include monomers, oligomers,polymers, gels, or combinations thereof. In some embodiments, thereagents include water, oxidants, reductants, acids, bases, orcombinations thereof. In some embodiments, the reagents be added in thepresence of catalysts such as acids, bases, or combinations thereof. Insome embodiments, the reagents are added during a time period of lessthan about 1 minute, less than about 1 hour, less than about 1 day, lessthan about 1 week, more than 1 minute, more than 1 hour, more than 1day, from about 1 minute to about 60 minutes, from about 1 hour to about24 hours, or from about 1 day to about 7 days. In some embodiments, thereagents are dripped into the reactor continuously or at intervals. Insome embodiments, multiple reagents are added to the reactor atdifferent rates. In some embodiments, some reagents are combinedseparately and reacted to form a gel or polymer prior to addition to thereactor.

In some embodiments, the freshly coated ion exchange material is heatedto one or more temperatures to age, dry, react, or crystallize thecoating. In some embodiments, the freshly coated ion exchange materialis heated to a temperature of less than about 100° C., less than about200° C., less than about 300° C., less than about 400° C., less thanabout 500° C., less than about 600° C., less than about 700° C., or lessthan about 800° C. In some embodiments, the freshly coated ion exchangematerial is heated to a temperature of more than about 100° C., morethan about 200° C., more than about 300° C., more than about 400° C.,more than about 500° C., more than about 600° C., more than about 700°C., or more than about 800° C. In some embodiments, the freshly coatedion exchange material is heated to a temperature from about 100° C. toabout 800° C., from about 200° C. to about 800° C., from about 300° C.to about 700° C., from about 400° C. to about 700° C., from about 500°C. to about 700° C., from about 100° C. to about 300° C., from about200° C. to about 400° C., from about 300° C. to about 500° C., fromabout 400° C. to about 600° C., from about 500° C. to about 700° C., orfrom about 600° C. to about 800° C. In some embodiments, the freshlycoated ion exchange material is heated in an atmosphere of aircomprising oxygen, nitrogen, hydrogen, argon, or combinations thereof.In some embodiments, the freshly coated ion exchange material is heatedfor a time period of less than about 1 hour, less than about 2 hours,less than about 4 hours, less than about 8 hours, less than about 24hours, more than 1 hour, more than 2 hours, more than 4 hours, more than8 hours, from about 0.5 hours to about 24 hours, from about 0.5 hours toabout 8 hours, from about 0.5 hours to about 4 hours, from about 0.5hours to about 2 hours, or from about 0.5 hours to about 1 hour.

In some embodiments, the coating material is deposited with physicalcharacteristics such as crystalline, amorphous, full coverage, partialcoverage, uniform, non-uniform, or combinations thereof. In someembodiments, multiple coatings are deposited on the ion exchangematerial in an arrangement such as concentric, patchwork, orcombinations thereof.

Ion Exchange Material of Coated Ion Exchange Particles in PorousStructure

In some embodiments, the ion exchange material is suitable for highlithium absorption capacity and for lithium ions in a liquid resourcerelative to other ions such as sodium ions and magnesium ions. In someembodiments, the ion exchange material is suitable for strong lithiumion uptake in liquid resources including those with low concentrationsof lithium ions, facile elution of lithium ions with a small excess ofacid, and fast ionic diffusion.

In some embodiments, the ion exchange material comprises an oxide, aphosphate, an oxyfluoride, a fluorophosphate, or combinations thereof.In a further embodiment, the ion exchange material comprises LiFePO₄,LiMnPO₄, Li₂MO₃ (M=Ti, Mn, Sn), Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiMO₂ (M=Al, Cu, Ti), Li₄TiO₄, Li₇Ti₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O, SnO₂.xSb₂O₅.yH₂O,TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, or combinations thereof. Insome embodiment, x is selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, y isselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, x and y is independentlyselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, an ion exchange materialcomprises LiFePO₄, Li₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂, Li₄Mn₅O₁₂,Li_(1.6)Mn_(1.6)O₄, solid solutions thereof, or combinations thereof.

In some embodiments, the ion exchange material is synthesized by amethod such as hydrothermal, solvothermal, sol-gel, solid state, moltensalt flux, ion exchange, microwave, ball milling, chemicalprecipitation, co-precipitation, vapor deposition, or combinationsthereof. In some embodiments, the ion exchange material is synthesizedby a method such as chemical precipitation, hydrothermal, solid state,microwave, or combinations thereof.

In some embodiments, the ion exchange materials are synthesized in alithiated state with a sub-lattice fully or partly occupied by lithiumions. In some embodiments, the ion exchange materials are synthesized ina hydrated state with a sub-lattice fully or partly occupied by hydrogenions.

In some embodiments, the ion exchange material and the coating materialform one or more concentration gradients where the chemical compositionof the coated ion exchange particle varies between two or morecompositions. In some embodiments, the chemical composition variesbetween the ion exchange materials and the coating in a manner that iscontinuous, discontinuous, or continuous and discontinuous in differentregions of the coated ion exchange particle. In some embodiments, theion exchange materials and the coating materials form a concentrationgradient that extends over a thickness of less than 1 nm, less than 10nm, less than 100 nm, less than 1,000nm, less than 10,000 nm, less than100,000 nm, more than 1 nm, more than 10 nm, more than 100 nm, more than1,000 nm, more than 10,000 nm, from about 1 nm to about 100,000 nm, fromabout 10 nm, to about 10,000 nm, or from about 100 to about 1,000 nm.

Particle Size of Coated Ion Exchange Particles In Porous structure

In some embodiments, the coated ion exchange particle has an averagediameter of less than about 10 nm, less than about 20 nm, less thanabout 30 nm, less than about 40 nm, less than about 50 nm, less thanabout 60 nm, less than about 70 nm, less than about 80 nm, less thanabout 90 nm, less than about 100 nm, less than about 1,000 nm, less thanabout 10,000 nm, less than about 100,000 nm, more than about 10 nm, morethan about 20 nm, more than about 30 nm, more than about 40 nm, morethan about 50 nm, more than about 60 nm, more than about 70 nm, morethan about 80 nm, more than about 90 nm, more than about 100 nm, morethan about 1,000 nm, more than about 10,000 nm, from about 1 nm to about10,000 nm, from about 1 nm to about 1,000 nm, from about 1 nm to about100 nm, from about 1 nm to about 80 nm, from about 1 nm to about 60 nm,from about 1 nm to about 40 nm, or from about 1 nm to about 20 nm. Insome embodiments, the coated ion exchange particles have an average sizeof less than about 100 nm, less than about 1,000 nm, or less than about10,000 nm. In some embodiments, the coated ion exchange particles aresecondary particles comprised of smaller primary particles, wherein thesecondary particles have an average diameter of less than about 10 nm,less than about 20 nm, less than about 30 nm, less than about 40 nm,less than about 50 nm, less than about 60 nm, less than about 70 nm,less than about 80 nm, less than about 90 nm, less than about 100 nm,less than about 1,000 nm, less than about 10,000 nm, less than about100,000 nm, more than about 10 nm, more than about 20 nm, more thanabout 30 nm, more than about 40 nm, more than about 50 nm, more thanabout 60 nm, more than about 70 nm, more than about 80 nm, more thanabout 90 nm, more than about 100 nm, more than about 1,000 nm, more thanabout 10,000 nm, from about 1 nm to about 10,000 nm, from about 1 nm toabout 1,000 nm, from about 1 nm to about 100 nm, from about 1 nm toabout 80 nm, from about 1 nm to about 60 nm, from about 1 nm to about 40nm, or from about 1 nm to about 20 nm.

In some embodiments, the coated ion exchange particle has an averagediameter of less than about 10 μm, less than about 20 μm, less thanabout 30 μm, less than about 40 μm, less than about 50 μm, less thanabout 60 μm, less than about 70 μm, less than about 80 μm, less thanabout 90 μm, less than about 100 μm, less than about 1,000 μm, less thanabout 10,000 μm, less than about 100,000 μm, more than about 10 μm, morethan about 20 μm, more than about 30 μm, more than about 40 μm, morethan about 50 μm, more than about 60 μm, more than about 70 μm, morethan about 80 μm, more than about 90 μm, more than about 100 μm, morethan about 1,000 μm, more than about 10,000 μm, from about 1 μm to about10,000 μm, from about 1 μm to about 1,000 μm, from about 1 μm to about100 μm, from about 1 μm to about 80 μm, from about 1 μm to about 60 μm,from about 1 μm to about 40 μm, or from about 1 μm to about 20 μm. Insome embodiments, the coated ion exchange particles have an average sizeof less than about 100 μm, less than about 1,000 μm, or less than about10,000 μm. In some embodiments, the coated ion exchange particles aresecondary particles comprised of smaller primary particles, wherein thesecondary particles have an average diameter of less than about 10 μm,less than about 20 μm, less than about 30 μm, less than about 40 μm,less than about 50 μm, less than about 60 μm, less than about 70 μm,less than about 80 μm, less than about 90 μm, less than about 100 μm,less than about 1,000 μm, less than about 10,000 μm, less than about100,000 μm, more than about 10 μm, more than about 20 μm, more thanabout 30 μm, more than about 40 μm, more than about 50 μm, more thanabout 60 μm, more than about 70 μm, more than about 80 μm, more thanabout 90 μm, more than about 100 μm, more than about 1,000 μm, more thanabout 10,000 μm, from about 1 μm to about 10,000 μm, from about 1 μm toabout 1,000 μm, from about 1 μm to about 100 μm, from about 1 μm toabout 80 μm, from about 1 μm to about 60 μm, from about 1 μm to about 40μm, or from about 1 μm to about 20

In an embodiment, the average diameter of the coated ion exchangeparticles or the average diameter of coated ion exchange particles whichare secondary particles comprised of smaller primary particles, isdetermined by measuring the particle size distribution of the coated ionexchange particles or the coated ion exchange particles which aresecondary particles comprised of smaller primary particles, anddetermining the mean particle size.

Uncoated Ion Exchange Particles in Porous Structure

In an aspect described herein, uncoated ion exchange particles areembedded in, adhered to, or otherwise supported by the structuralsupport.

Ion Exchange Material of Uncoated Ion Exchange Particles in PorousStructure

In some embodiments, the ion exchange material is suitable for highlithium absorption capacity and for lithium ions in a liquid resourcerelative to other ions such as sodium ions and magnesium ions. In someembodiments, the ion exchange material is suitable for strong lithiumion uptake in liquid resources including those with low concentrationsof lithium ions, facile elution of lithium ions with a small excess ofacid, and fast ionic diffusion.

In some embodiments, the ion exchange material comprises an oxide, aphosphate, an oxyfluoride, a fluorophosphate, or combinations thereof.In a further embodiment, the ion exchange material comprises LiFePO₄,LiMnPO₄, Li₂MO₃ (M=Ti, Mn, Sn), Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiMO₂ (M=Al, Cu, Ti), Li₄TiO₄, Li₇Ti₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O, SnO₂.xSb₂O₅.yH₂O,TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, or combinations thereof. Insome embodiment, x is selected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7,0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, and 10. In some embodiments, y isselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, x and y is independentlyselected from 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4,5, 6, 7, 8, 9, and 10. In some embodiments, an ion exchange materialcomprises LiFePO₄, Li₂SnO₃, Li₂MnO₃, Li₂TiO₃, Li₄Ti₅O₁₂, Li₄Mn₅O₁₂,Li_(1.6)Mn_(1.6)O₄, solid solutions thereof, or combinations thereof.

In some embodiments, the ion exchange material is synthesized by amethod such as hydrothermal, solvothermal, sol-gel, solid state, moltensalt flux, ion exchange, microwave, ball milling, chemicalprecipitation, co-precipitation, vapor deposition, or combinationsthereof. In some embodiments, the ion exchange material is synthesizedby a method such as chemical precipitation, hydrothermal, solid state,microwave, or combinations thereof.

In some embodiments, the ion exchange materials are synthesized in alithiated state with a sub-lattice fully or partly occupied by lithiumions. In some embodiments, the ion exchange materials are synthesized ina hydrated state with a sub-lattice fully or partly occupied by hydrogenions.

Particle Size of Uncoated Ion Exchange Particles in Porous Structure

In some embodiments, the uncoated ion exchange particle has an averagediameter of less than about 10 nm, less than about 20 nm, less thanabout 30 nm, less than about 40 nm, less than about 50 nm, less thanabout 60 nm, less than about 70 nm, less than about 80 nm, less thanabout 90 nm, less than about 100 nm, less than about 1,000 nm, less thanabout 10,000 nm, less than about 100,000 nm, more than about 10 nm, morethan about 20 nm, more than about 30 nm, more than about 40 nm, morethan about 50 nm, more than about 60 nm, more than about 70 nm, morethan about 80 nm, more than about 90 nm, more than about 100 nm, morethan about 1,000 nm, more than about 10,000 nm, from about 1 nm to about10,000 nm, from about 1 nm to about 1,000 nm, from about 1 nm to about100 nm, from about 1 nm to about 80 nm, from about 1 nm to about 60 nm,from about 1 nm to about 40 nm, or from about 1 nm to about 20 nm. Insome embodiments, the uncoated ion exchange particles have an averagesize of less than about 100 nm, less than about 1,000 nm, or less thanabout 10,000 nm. In some embodiments, the uncoated ion exchangeparticles are secondary particles comprised of smaller primaryparticles, wherein the secondary particles have an average diameter ofless than about 10 nm, less than about 20 nm, less than about 30 nm,less than about 40 nm, less than about 50 nm, less than about 60 nm,less than about 70 nm, less than about 80 nm, less than about 90 nm,less than about 100 nm, less than about 1,000 nm, less than about 10,000nm, less than about 100,000 nm, more than about 10 nm, more than about20 nm, more than about 30 nm, more than about 40 nm, more than about 50nm, more than about 60 nm, more than about 70 nm, more than about 80 nm,more than about 90 nm, more than about 100 nm, more than about 1,000 nm,more than about 10,000 nm, from about 1 nm to about 10,000 nm, fromabout 1 nm to about 1,000 nm, from about 1 nm to about 100 nm, fromabout 1 nm to about 80 nm, from about 1 nm to about 60 nm, from about 1nm to about 40 nm, or from about 1 nm to about 20 nm.

In some embodiments, the uncoated ion exchange particle has an averagediameter of less than about 10 μm, less than about 20 μm, less thanabout 30 μm, less than about 40 μm, less than about 50 μm, less thanabout 60 μm, less than about 70 μm, less than about 80 μm, less thanabout 90 μm, less than about 100 μm, less than about 1,000 μm, less thanabout 10,000 μm, less than about 100,000 μm, more than about 10 μm, morethan about 20 μm, more than about 30 μm, more than about 40 μm, morethan about 50 μm, more than about 60 μm, more than about 70 μm, morethan about 80 μm, more than about 90 μm, more than about 100 μm, morethan about 1,000 μm, more than about 10,000 μm, from about 1 μm to about10,000 μm, from about 1 μm to about 1,000 μm, from about 1 μm to about100 μm, from about 1 μm to about 80 μm, from about 1 μm to about 60 μm,from about 1 μm to about 40 μm, or from about 1 μm to about 20 μm. Insome embodiments, the uncoated ion exchange particles have an averagesize of less than about 100 μm, less than about 1,000 μm, or less thanabout 10,000 μm. In some embodiments, the uncoated ion exchangeparticles are secondary particles comprised of smaller primaryparticles, wherein the secondary particles have an average diameter ofless than about 10 μm, less than about 20 μm, less than about 30 μm,less than about 40 μm, less than about 50 μm, less than about 60 μm,less than about 70 μm, less than about 80 μm, less than about 90 μm,less than about 100 μm, less than about 1,000 μm, less than about 10,000μm, less than about 100,000 μm, more than about 10 μm, more than about20 μm, more than about 30 μm, more than about 40 μm, more than about 50μm, more than about 60 μm, more than about 70 μm, more than about 80 μm,more than about 90 μm, more than about 100 μm, more than about 1,000 μm,more than about 10,000 μm, from about 1 μm to about 10,000 μm, fromabout 1 μm to about 1,000 μm, from about 1 μm to about 100 μm, fromabout 1 μm to about 80 μm, from about 1 μm to about 60 μm, from about 1μm to about 40 μm, or from about 1 μm to about 20 μm.

In an embodiment, the average diameter of the uncoated ion exchangeparticles or the average diameter of the uncoated ion exchange particleswhich are secondary particles comprised of smaller primary particles, isdetermined by measuring the particle size distribution of the uncoatedion exchange particles or the uncoated ion exchange particles which aresecondary particles comprised of smaller primary particles, anddetermining the mean particle size.

Porous Beads

In an aspect described herein, the porous structure is in the form of aporous bead.

In some embodiments, the porous bead is formed from dry powder using amechanical press, a pellet press, a tablet press, a pill press, a rotarypress, or combinations thereof. In some embodiments, the porous bead isformed from a solvent slurry by dripping the slurry into a differentliquid solution. The solvent slurry is formed using a solvent ofN-methyl-2-pyrrolidone, dimethyl sulfoxide, tetrahydrofuran,dimethylformamide, dimethylacetamide, methyl ethyl ketone, orcombinations thereof. The different liquid solutions comprise water,ethanol, iso-propyl alcohol, acetone, or combinations thereof.

Spherical Beads

In some embodiments, the porous bead is approximately spherical with anaverage diameter of less than 10 μm, less than 100 μm, less than 1 mm,less than 1 cm, less than 10 cm, more than 10 μm, more than 100 μm, morethan 1 mm, more than 1 cm, from about 1 μm to about 100 μm, from about 1mm to about 100 mm, from about 1 mm to about 80 mm, from about 1 mm toabout 60 mm, from about 1 to about 40 mm, from about 1 to about 20 mm,from about 1 to about 10 mm, from about 1 cm to about 10 cm, from about1 cm to about 8 cm, from about 1 cm to about 6 cm, or from about 1 cm toabout 4 cm. In some embodiments, the porous bead is approximatelyspherical with an average diameter of less than 200 μm, less than 2 mm,less than 20 mm, more than 200 μm, more than 2 mm, more than 20 mm, fromabout 1 μ to about 100 μm, from about 1 μm to about 200 μm, from about 1μm to about 2 mm, from about 1 μm to about 20 mm, or from about 2 mm toabout 200 mm.

Tablet-shaped Beads

In some embodiments, the porous bead is tablet-shaped with a diameter ofless than 1 mm, less than 2 mm, less than 4 mm, less than 8 mm, lessthan 20 mm, more than 1 mm, more than 2 mm, more than 4 mm, more than 8mm, from about 0.5 mm to about 1 mm, from about 0.5 mm to about 2 mm,from about 1 mm to about 4 mm, from about 1 mm to about 8 mm, from about1 mm to about 20 mm, and with a height of less than 1 mm, less than 2mm, less than 4 mm, less than 8 mm, less than 20 mm, more than 1 mm,more than 2 mm, more than 4 mm, more than 8 mm, from about 0.5 mm toabout 1 mm, from about 0.5 mm to about 2 mm, from about 1 mm to about 4mm, from about 1 mm to about 8 mm, from about 1 mm to about 20 mm. Insome embodiments, the porous bead has a diameter of less than 8 mm and aheight of less than 8 mm. In some embodiments, the porous bead has adiameter of less than 4 mm and a height of less than 4 mm. In someembodiments, the porous bead has a diameter of less than 2 mm and aheight of less than 2 mm. In some embodiments, the porous bead has adiameter of less than 1 mm and a height of less than 1 mm.

Methods

Methods Using Coated Ion Exchange Particles

In an aspect described herein are methods of extracting lithium from aliquid resource, comprising contacting the coated ion exchange particleswith a liquid resource to produce lithiated coated ion exchangeparticles; and treating the lithiated coated ion exchange particles withan acid solution to produce a salt solution comprising lithium ions.Here, the coated ion exchange particles are optionally mixed with aliquid resource to absorb lithium and then recovered through filtration,gravimetric separation, or other means.

In some embodiments, the liquid resource is a natural brine, a dissolvedsalt flat, seawater, concentrated seawater, desalination effluent, aconcentrated brine, a processed brine, liquid from an ion exchangeprocess, liquid from a solvent extraction process, a synthetic brine,leachate from ores, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, waterfrom an oilfield, effluent from a chemical process, or combinationsthereof. In some embodiments, a liquid resource is a natural brine, adissolved salt flat, a concentrated brine, water from an oilfield, aprocessed brine, a synthetic brine, liquid from an ion exchange process,liquid from a solvent extraction process, leachate from minerals,leachate from clays, leachate from recycled products, leachate fromrecycled materials, or combinations thereof. In some embodiments, the pHof the brine is adjusted before or after ion exchange to neutralizeacidic protons released by the ion exchange material during lithiumuptake.

In some embodiments, the liquid resource has a lithium ion concentrationof less than about 100,000 ppm, less than about 10,000 ppm, less thanabout 1,000 ppm, less than about 100 ppm, less than about 10 ppm, orcombinations thereof. In some embodiments, the liquid resource has alithium ion concentration less than about 5,000 ppm, less than about 500ppm, less than about 50 ppm, or combinations thereof. In someembodiments, the liquid resource has sodium ion, calcium ion, magnesiumion, potassium ion, or strontium ion concentrations greater than about100 ppm, greater than about 1,000 ppm, greater than about 10,000 ppm, orgreater than about 100,000 ppm. In some embodiments, the liquid resourcehas hydrocarbon, hydrogen sulfide, surfactant, or microbe concentrationsgreater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, 1,000 ppm, or 10,000ppm. In some embodiments, the liquid resource has suspended solids at aconcentration of greater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, or1,000 ppm.

In some embodiments, the acid solution used for recovering lithium ionsfrom the coated ion exchange particles is prepared with hydrochloricacid, sulfuric acid, phosphoric acid, hydrobromic acid, chloric acid,perchloric acid, nitric acid, formic acid, acetic acid, or combinationsthereof. In some embodiments, the acid solution is prepared withhydrochloric acid, sulfuric acid, nitric phosphoric acid, orcombinations thereof. In some embodiments, the acid solution has an acidconcentration greater than about 0.1 M, greater than about 0.5 M,greater than about 1 M, greater than about 5 M, or greater than about 10M, or combinations thereof. In some embodiments, the acid solution hasan acid concentration lesser than about 0.1 M, lesser than about 0.5 M,lesser than about 1 M, lesser than about 5 M, or lesser than about 10 M,or combinations thereof. In some embodiments, the acid solution has anacid concentration from about 0.1 M to about 10 M, from about 0.5 M toabout 5 M, or from about 0.5 M to about 1 M. In some embodiments, theacid solution has a pH less than about 4, less than about 2, less thanabout 1, or less than about 0. In some embodiments, the acid solutionhas a pH that increases over time as the acid solution is exposed to thecoated ion exchange particles and the coated ion exchange particlesabsorb protons while releasing lithium ions.

In some embodiments, the coated ion exchange particles perform the ionexchange reaction repeatedly over a number of cycles greater than about10 cycles, greater than about 30 cycles, greater than about 100 cycles,or greater than about 300 cycles. In some embodiments, the coated ionexchange particles are used until their lithium uptake capacity drops bygreater than about 5%, greater than about 10%, greater than about 20%,greater than about 40%, or greater than about 60% below their initiallithium uptake capacity. In some embodiments, the coated ion exchangeparticles are used until their lithium uptake capacity drops by lesserthan about 5%, lesser than about 10%, lesser than about 20%, lesser thanabout 40%, or lesser than about 60% below their initial lithium uptakecapacity.

In some embodiments, the coated ion exchange particles are comprised ofan ion exchange material and a coating material wherein the ion exchangematerial comprises Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, Li₂MO₃ (M=Ti, Mn, Sn),LiFePO₄, solid solutions thereof, or combinations thereof and thecoating material comprises TiO₂, ZrO₂, SiO₂ MoO₂, ZrSiO₄, Li₂TiO₃,Li₂ZrO₃, LiNbO₃, AlF₃, SiC, Si₃N₄, graphitic carbon, amorphous carbon,diamond-like carbon-carbon, or combinations thereof. The coated ionexchange particles have an average diameter less than about 10 nm, lessthan about 20 nm, less than about 30 nm, less than about 40 nm, lessthan about 50 nm, less than about 60 nm, less than about 70 nm, lessthan about 80 nm, less than about 90 nm, less than about 100 nm, lessthan about 1,000 nm, less than about 10,000 nm, less than about 100,000nm, more than about 10 nm, more than about 20 nm, more than about 30 nm,more than about 40 nm, more than about 50 nm, more than about 60 nm,more than about 70 nm, more than about 80 nm, more than about 90 nm,more than about 100 nm, more than about 1,000 nm, more than about 10,000nm, from about 1 nm to about 10,000 nm, from about 1 nm to about 1,000nm, from about 1 nm to about 100 nm, from about 1 nm to about 80 nm,from about 1 nm to about 60 nm, from about 1 nm to about 40 nm, or fromabout 1 nm to about 20 nm, and the coating thickness is less than 1 nm,less than 10 nm, less than 100 nm, less than 1,000 nm, less than 10,000nm, more than 1 nm, more than 10 nm, more than 100 nm, more than 1,000nm, more than 10,000 nm, from about 1 nm to about 10,000 nm, from about10 nm, to about 1,000 nm, or from about 100 to about 1,000nm. In someembodiments, the coating material has a thickness of less than 5 nm,less than 10 nm, less than 50 nm, less than 100 nm, less than 500 nm,more than 1 nm, more than 5 nm, more than 10 nm, more than 50 nm, morethan 100 nm, from about 1 nm to about 500 nm, from about 1 nm to about100 nm, from about 1 nm to about 50 nm, from about 1 nm to about 10 nm,from about 1 nm to about 5 nm, or from about 5 nm to about 100 nm. Thecoated ion exchange particles are created by synthesizing the ionexchange material using a method such as hydrothermal, solid state,microwave, or combinations thereof. The coating material is deposited onthe surface of the ion exchange material using a method such as chemicalvapor deposition, hydrothermal, solvothermal, sol-gel, precipitation,microwave or by suspending the ion exchange material in a solvent andthen adding reagents including metal chloride, metal oxychloride, metalalkoxide, water, acid, base, or combinations thereof. The coated ionexchange particles are treated with an acid solution prepared withhydrochloric acid, sulfuric acid, nitric acid, or combinations thereofwherein the concentration of the acid solution is greater than about 0.1M, greater than about 0.5 M, greater than about 2 M, greater than about5 M, or combinations thereof. During acid treatment, the coated ionexchange particles absorb hydrogen ions while releasing lithium ions.The ion exchange material is converted to a protonated state. Thecoating material allows diffusion of hydrogen ions and lithium ionsrespectively to and from the ion exchange material while providing aprotective barrier that limits dissolution of the ion exchange material.After treatment in acid, the protonated coated ion exchange particlesare treated with a liquid resource wherein the liquid resource is anatural brine, a dissolved salt flat, a concentrated brine, a processedbrine, a synthetic brine, an oilfield brine, liquid from an ion exchangeprocess, liquid from a solvent extraction process, leachate fromminerals, leachate from clays, leachate from recycled products, leachatefrom recycled materials, or combinations thereof. The coated ionexchange particles absorb lithium ions while releasing hydrogen ions.After acid treatment, the lithium salt solution is collected andprocessed into lithium carbonate, lithium hydroxide, or lithiumphosphate.

Methods Using Porous Structure

In an aspect described herein are methods of extracting lithium from aliquid resource, comprising contacting the porous structure with aliquid resource to produce a lithiated porous structure, and treatingthe lithiated porous structure with an acid solution to produce a saltsolution comprising lithium ions.

In some embodiments, the liquid resource is a natural brine, a dissolvedsalt flat, seawater, concentrated seawater, desalination effluent, aconcentrated brine, a processed brine, liquid from an ion exchangeprocess, liquid from a solvent extraction process, a synthetic brine,leachate from ores, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, waterfrom an oilfield, effluent from a chemical process, or combinationsthereof. In some embodiments, a liquid resource is a natural brine, adissolved salt flat, a concentrated brine, water from an oilfield, aprocessed brine, a synthetic brine, liquid from an ion exchange process,liquid from a solvent extraction process, leachate from minerals,leachate from clays, leachate from recycled products, leachate fromrecycled materials, or combinations thereof. In some embodiments, the pHof the brine is adjusted before or after ion exchange to neutralizeacidic protons released during lithium uptake.

In some embodiments, the liquid resource has a lithium ion concentrationof less than about 100,000 ppm, less than about 10,000 ppm, less thanabout 1,000 ppm, less than about 100 ppm, less than about 10 ppm, orcombinations thereof. In some embodiments, the liquid resource has alithium ion concentration less than about 5,000 ppm, less than about 500ppm, less than about 50 ppm, or combinations thereof. In someembodiments, the liquid resource has sodium ion, calcium ion, magnesiumion, potassium ion, or strontium ion concentrations greater than about100 ppm, greater than about 1,000 ppm, greater than about 10,000 ppm, orgreater than about 100,000 ppm. In some embodiments, the liquid resourcehas hydrocarbon, hydrogen sulfide, surfactant, or microbe concentrationsgreater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, 1,000 ppm, or 10,000ppm. In some embodiments, the liquid resource has suspended solids at aconcentration of greater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, or1,000 ppm.

In some embodiments, the acid solution used for recovering lithium ionsfrom the porous structure is prepared with hydrochloric acid, sulfuricacid, phosphoric acid, hydrobromic acid, chloric acid, perchloric acid,nitric acid, formic acid, acetic acid, or combinations thereof. In someembodiments, the acid solution is prepared with hydrochloric acid,sulfuric acid, nitric phosphoric acid, or combinations thereof. In someembodiments, the acid solution has an acid concentration greater thanabout 0.1 M, greater than about 0.5 M, greater than about 1 M, greaterthan about 5 M, or greater than about 10 M, or combinations thereof. Insome embodiments, the acid solution has an acid concentration lesserthan about 0.1 M, lesser than about 0.5 M, lesser than about 1 M, lesserthan about 5 M, or lesser than about 10 M, or combinations thereof. Insome embodiments, the acid solution has an acid concentration from about0.1 M to about 10 M, from about 0.5 M to about 5 M, or from about 0.5 Mto about 1 M. In some embodiments, the acid solution has a pH less thanabout 4, less than about 2, less than about 1, or less than about 0. Insome embodiments, the acid solution has a pH that increases over time asthe acid solution is exposed to the porous structure and the porousstructure absorbs protons while releasing lithium ions.

In some embodiments, the porous structure performs the ion exchangereaction repeatedly over a number of cycles greater than 10 cycles,greater than 30 cycles, greater than 100 cycles, greater than 300cycles, or greater than 1,000 cycles. In some embodiments, the porousstructure performs the ion exchange reaction repeatedly over a number ofcycles greater than 50 cycles, greater than 100 cycles, or greater than200 cycles.

In some embodiments, the coated ion exchange particles, the uncoated ionexchange particles, and combinations thereof in the porous structureperform the ion exchange reaction repeatedly over a number of cyclesgreater than about 10 cycles, greater than about 30 cycles, greater thanabout 100 cycles, or greater than about 300 cycles. In some embodiments,the coated ion exchange particles, the uncoated ion exchange particles,and combinations thereof in the porous bead are used until lithiumuptake capacity drops by greater than about 5%, greater than about 10%,greater than about 20%, greater than about 40%, or greater than about60% below their initial lithium uptake capacity. In some embodiments,the coated ion exchange particles are used until their lithium uptakecapacity drops by lesser than about 5%, lesser than about 10%, lesserthan about 20%, lesser than about 40%, or lesser than about 60% belowtheir initial lithium uptake capacity.

In some embodiments, the coated ion exchange particles of the porousstructure are comprised of an ion exchange material and a coatingmaterial wherein the ion exchange material comprises Li₄Mn₅O₁₂,Li_(1.6)Mn_(1.6)O₄, Li₂MO₃ (M=Ti, Mn, Sn), LiFePO₄, solid solutionsthereof, or combinations thereof and the coating material comprisesTiO₂, ZrO₂, SiO₂ MoO₂, ZrSiO₄, Li₂TiO₃, Li₂ZrO₃, LiNbO₃, AlF₃, SiC,Si₃N₄, graphitic carbon, amorphous carbon, diamond-like carbon-carbon,or combinations thereof. The coated ion exchange particles of the porousstructure have an average diameter less than about 10 nm, less thanabout 20 nm, less than about 30 nm, less than about 40 nm, less thanabout 50 nm, less than about 60 nm, less than about 70 nm, less thanabout 80 nm, less than about 90 nm, less than about 100 nm, less thanabout 1,000 nm, less than about 10,000 nm, less than about 100,000 nm,more than about 10 nm, more than about 20 nm, more than about 30 nm,more than about 40 nm, more than about 50 nm, more than about 60 nm,more than about 70 nm, more than about 80 nm, more than about 90 nm,more than about 100 nm, more than about 1,000 nm, more than about 10,000nm, from about 1 nm to about 10,000 nm, from about 1 nm to about 1,000nm, from about 1 nm to about 100 nm, from about 1 nm to about 80 nm,from about 1 nm to about 60 nm, from about 1 nm to about 40 nm, or fromabout 1 nm to about 20 nm, and the coating thickness is less than 1 nm,less than 10 nm, less than 100 nm, less than 1,000 nm, less than 10,000nm, more than 1 nm, more than 10 nm, more than 100 nm, more than 1,000nm, more than 10,000 nm, from about 1 nm to about 10,000 nm, from about10 nm, to about 1,000 nm, or from about 100 to about 1,000 nm. In someembodiments, the coating material has a thickness of less than 5 nm,less than 10 nm, less than 50 nm, less than 100 nm, less than 500 nm,more than 1 nm, more than 5 nm, more than 10 nm, more than 50 nm, morethan 100 nm, from about 1 nm to about 500 nm, from about 1 nm to about100 nm, from about 1 nm to about 50 nm, from about 1 nm to about 10 nm,from about 1 nm to about 5 nm, or from about 5 nm to about 100 nm. Thecoated ion exchange particles of the porous structure are created byfirst synthesizing the ion exchange material using a method such ashydrothermal, solid state, microwave, or combinations thereof. Thecoating material is deposited on the surface of the ion exchangematerial using a method such as chemical vapor deposition, hydrothermal,solvothermal, sol-gel, precipitation, or microwave by suspending the ionexchange material in a solvent and then adding reagents including metalchloride, metal oxychloride, metal alkoxide, water, acid, base, orcombinations thereof. The coated ion exchange particles of the porousstructure is treated with an acid solution prepared with hydrochloricacid, sulfuric acid, nitric acid, or combinations thereof wherein theconcentration of the acid solution is greater than about 0.1 M, greaterthan about 0.5 M, greater than about 2 M, greater than about 5 M, orcombinations thereof. During acid treatment, the coated ion exchangeparticles of the porous structure absorb hydrogen ions while releasinglithium ions. The ion exchange material is converted to a protonatedstate. The coating material allows diffusion of hydrogen ions andlithium ions respectively to and from the ion exchange material whileproviding a protective barrier that limits dissolution of the ionexchange material. After treatment in acid, the protonated coated ionexchange particles of the porous structure are treated with a liquidresource wherein the liquid resource is a natural brine, a dissolvedsalt flat, a concentrated brine, a processed brine, a synthetic brine,an oilfield brine, liquid from an ion exchange process, liquid from asolvent extraction process, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, orcombinations thereof. The coated ion exchange particles of the porousstructure absorb lithium ions while releasing hydrogen ions. After acidtreatment, the lithium salt solution is collected and processed intolithium carbonate, lithium hydroxide, or lithium phosphate.

In an embodiment, the uncoated ion exchange particles of the porousstructure are comprised of an ion exchange material wherein the ionexchange material comprises Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, Li₂MO₃ (M=Ti,Mn, Sn), LiFePO₄, solid solutions thereof, or combinations thereof. Theuncoated ion exchange particles of the porous structure have an averagediameter less than about 10 nm, less than about 20 nm, less than about30 nm, less than about 40 nm, less than about 50 nm, less than about 60nm, less than about 70 nm, less than about 80 nm, less than about 90 nm,less than about 100 nm, less than about 1,000 nm, less than about 10,000nm, less than about 100,000 nm, more than about 10 nm, more than about20 nm, more than about 30 nm, more than about 40 nm, more than about 50nm, more than about 60 nm, more than about 70 nm, more than about 80 nm,more than about 90 nm, more than about 100 nm, more than about 1,000 nm,more than about 10,000 nm, from about 1 nm to about 10,000 nm, fromabout 1 nm to about 1,000 nm, from about 1 nm to about 100 nm, fromabout 1 nm to about 80 nm, from about 1 nm to about 60 nm, from about 1nm to about 40 nm, or from about 1 nm to about 20 nm. The uncoated ionexchange particles of the porous structure are created by synthesizingthe ion exchange material using a method such as hydrothermal, solidstate, microwave, or combinations thereof. The uncoated ion exchangeparticles of the porous structure is treated with an acid solutionprepared with hydrochloric acid, sulfuric acid, nitric acid, orcombinations thereof wherein the concentration of the acid solution isgreater than about 0.1 M, greater than about 0.5 M, greater than about 2M, greater than about 5 M, or combinations thereof. During acidtreatment, the uncoated ion exchange particles of the porous structureabsorb hydrogen ions while releasing lithium ions. The ion exchangematerial is converted to a protonated state. After treatment in acid,the protonated uncoated ion exchange particles are treated with a liquidresource wherein the liquid resource is a natural brine, a dissolvedsalt flat, a concentrated brine, a processed brine, a synthetic brine,an oilfield brine, liquid from an ion exchange process, liquid from asolvent extraction process, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, orcombinations thereof. The uncoated ion exchange particles absorb lithiumions while releasing hydrogen ions. After acid treatment, the lithiumsalt solution is collected and processed into lithium carbonate, lithiumhydroxide, or lithium phosphate.

In an embodiment, there is a combination of coated ion exchangeparticles and uncoated ion exchange particles in the porous structure.The combination of coated ion exchange particles and uncoated ionexchange particles in the porous structure is treated with an acidsolution prepared with hydrochloric acid, sulfuric acid, nitric acid, orcombinations thereof wherein the concentration of the acid solution isgreater than about 0.1 M, greater than about 0.5 M, greater than about 2M, greater than about 5 M, lesser than about 0.1 M, lesser than about0.5 M, lesser than about 1 M, lesser than about 5 M, or lesser thanabout 10 M, from about 0.1 M to about 10 M, from about 0.5 M to about 5M, or from about 0.5 M to about 1 M, or combinations thereof. Duringacid treatment, the combination of coated ion exchange particles anduncoated ion exchange particles in the porous structure absorb hydrogenions while releasing lithium ions. The ion exchange material isconverted to a protonated state. After treatment in acid, thecombination of protonated coated ion exchange particles and protonateduncoated ion exchange particles are treated with a liquid resourcewherein the liquid resource is a natural brine, a dissolved salt flat, aconcentrated brine, a processed brine, a synthetic brine, an oilfieldbrine, liquid from an ion exchange process, liquid from a solventextraction process, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, orcombinations thereof. The combination of protonated coated ion exchangeparticles and protonated uncoated ion exchange particles in the porousstructure absorb lithium ions while releasing hydrogen ions. After acidtreatment, the lithium salt solution is collected and processed intolithium carbonate, lithium hydroxide, or lithium phosphate.

Methods Using Porous Beads

In an aspect described herein are methods of extracting lithium from aliquid resource, comprising contacting the porous bead with a liquidresource to produce lithiated porous beads; and treating the lithiatedporous beads with an acid solution to produce a salt solution comprisinglithium ions.

In some embodiments, the liquid resource is a natural brine, a dissolvedsalt flat, seawater, concentrated seawater, desalination effluent, aconcentrated brine, a processed brine, liquid from an ion exchangeprocess, liquid from a solvent extraction process, a synthetic brine,leachate from ores, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, waterfrom an oilfield, effluent from a chemical process, or combinationsthereof. In some embodiments, a liquid resource is a natural brine, adissolved salt flat, a concentrated brine, water from an oilfield, aprocessed brine, a synthetic brine, liquid from an ion exchange process,liquid from a solvent extraction process, leachate from minerals,leachate from clays, leachate from recycled products, leachate fromrecycled materials, or combinations thereof. In some embodiments, the pHof the brine is adjusted before or after ion exchange to neutralizeacidic protons released during lithium uptake.

In some embodiments, the liquid resource has a lithium ion concentrationof less than about 100,000 ppm, less than about 10,000 ppm, less thanabout 1,000 ppm, less than about 100 ppm, less than about 10 ppm, orcombinations thereof. In some embodiments, the liquid resource has alithium ion concentration less than about 5,000 ppm, less than about 500ppm, less than about 50 ppm, or combinations thereof. In someembodiments, the liquid resource has sodium ion, calcium ion, magnesiumion, potassium ion, or strontium ion concentrations greater than about100 ppm, greater than about 1,000 ppm, greater than about 10,000 ppm, orgreater than about 100,000 ppm. In some embodiments, the liquid resourcehas hydrocarbon, hydrogen sulfide, surfactant, or microbe concentrationsgreater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, 1,000 ppm, or 10,000ppm. In some embodiments, the liquid resource has suspended solids at aconcentration of greater than about 1 ppb, 1 ppm, 10 ppm, 100 ppm, or1,000 ppm.

In some embodiments, the acid solution used for recovering lithium ionsfrom the porous beads are prepared with hydrochloric acid, sulfuricacid, phosphoric acid, hydrobromic acid, chloric acid, perchloric acid,nitric acid, formic acid, acetic acid, or combinations thereof. In someembodiments, the acid solution is prepared with hydrochloric acid,sulfuric acid, nitric phosphoric acid, or combinations thereof. In someembodiments, the acid solution has an acid concentration greater thanabout 0.1 M, greater than about 0.5 M, greater than about 1 M, greaterthan about 5 M, or greater than about 10 M, or combinations thereof. Insome embodiments, the acid solution has an acid concentration lesserthan about 0.1 M, lesser than about 0.5 M, lesser than about 1 M, lesserthan about 5 M, or lesser than about 10 M, or combinations thereof. Insome embodiments, the acid solution has an acid concentration from about0.1 M to about 10 M, from about 0.5 M to about 5 M, or from about 0.5 Mto about 1 M. In some embodiments, the acid solution has a pH less thanabout 4, less than about 2, less than about 1, or less than about 0. Insome embodiments, the acid solution has a pH that increases over time asthe acid solution is exposed to the porous beads and the porous beadsabsorb protons while releasing lithium ions.

In some embodiments, the porous bead performs the ion exchange reactionrepeatedly over a number of cycles greater than 10 cycles, greater than30 cycles, greater than 100 cycles, greater than 300 cycles, or greaterthan 1,000 cycles. In some embodiments, the porous bead performs the ionexchange reaction repeatedly over a number of cycles greater than 50cycles, greater than 100 cycles, or greater than 200 cycles.

In some embodiments, the coated ion exchange particles, the uncoated ionexchange particles, and combinations thereof in the porous bead performthe ion exchange reaction repeatedly over a number of cycles greaterthan about 10 cycles, greater than about 30 cycles, greater than about100 cycles, or greater than about 300 cycles. In some embodiments, thecoated ion exchange particles, the uncoated ion exchange particles, andcombinations thereof in the porous bead are used until lithium uptakecapacity drops by greater than about 5%, greater than about 10%, greaterthan about 20%, greater than about 40%, or greater than about 60% belowtheir initial lithium uptake capacity. In some embodiments, the coatedion exchange particles are used until their lithium uptake capacitydrops by lesser than about 5%, lesser than about 10%, lesser than about20%, lesser than about 40%, or lesser than about 60% below their initiallithium uptake capacity.

In some embodiments, the coated ion exchange particles of the porousbead are comprised of an ion exchange material and a coating materialwherein the ion exchange material comprises Li₄Mn₅O₁₂,Li_(1.6)Mn_(1.6)O₄, Li₂MO₃ (M=Ti, Mn, Sn), LiFePO₄, solid solutionsthereof, or combinations thereof and the coating material comprisesTiO₂, ZrO₂, SiO₂ MoO₂, ZrSiO₄, Li₂TiO₃, Li₂ZrO₃, LiNbO₃, AlF₃, SiC,Si₃N₄, graphitic carbon, amorphous carbon, diamond-like carbon-carbon,or combinations thereof. The coated ion exchange particles of the porousbead have an average diameter less than about 10 nm, less than about 20nm, less than about 30 nm, less than about 40 nm, less than about 50 nm,less than about 60 nm, less than about 70 nm, less than about 80 nm,less than about 90 nm, less than about 100 nm, less than about 1,000 nm,less than about 10,000 nm, less than about 100,000 nm, more than about10 nm, more than about 20 nm, more than about 30 nm, more than about 40nm, more than about 50 nm, more than about 60 nm, more than about 70 nm,more than about 80 nm, more than about 90 nm, more than about 100 nm,more than about 1,000 nm, more than about 10,000 nm, from about 1 nm toabout 10,000 nm, from about 1 nm to about 1,000 nm, from about 1 nm toabout 100 nm, from about 1 nm to about 80 nm, from about 1 nm to about60 nm, from about 1 nm to about 40 nm, or from about 1 nm to about 20nm, and the coating thickness is less than 5 nm, less than 10 nm, lessthan 50 nm, less than 100 nm, less than 500 nm, more than 1 nm, morethan 5 nm, more than 10 nm, more than 50 nm, more than 100 nm, fromabout 1 nm to about 500 nm, from about 1 nm to about 100 nm, from about1 nm to about 50 nm, from about 1 nm to about 10 nm, from about 1 nm toabout 5 nm, or from about 5 nm to about 100 nm. The coated ion exchangeparticles of the porous bead are created by first synthesizing the ionexchange material using a method such as hydrothermal, solid state,microwave, or combinations thereof. The coating material is deposited onthe surface of the ion exchange material using a method such as chemicalvapor deposition, hydrothermal, solvothermal, sol-gel, precipitation, ormicrowave by suspending the ion exchange material in a solvent and thenadding reagents including metal chloride, metal oxychloride, metalalkoxide, water, acid, base, or combinations thereof. The coated ionexchange particles of the porous bead is treated with an acid solutionprepared with hydrochloric acid, sulfuric acid, nitric acid, orcombinations thereof wherein the concentration of the acid solution isgreater than about 0.1 M, greater than about 0.5 M, greater than about 2M, greater than about 5 M, or combinations thereof. During acidtreatment, the coated ion exchange particles of the porous bead absorbhydrogen ions while releasing lithium ions. The ion exchange material isconverted to a protonated state. The coating material allows diffusionof hydrogen ions and lithium ions respectively to and from the ionexchange material while providing a protective barrier that limitsdissolution of the ion exchange material. After treatment in acid, theprotonated coated ion exchange particles of the porous bead are treatedwith a liquid resource wherein the liquid resource is a natural brine, adissolved salt flat, a concentrated brine, a processed brine, asynthetic brine, an oilfield brine, liquid from an ion exchange process,liquid from a solvent extraction process, leachate from minerals,leachate from clays, leachate from recycled products, leachate fromrecycled materials, or combinations thereof. The coated ion exchangeparticles of the porous bead absorb lithium ions while releasinghydrogen ions. After acid treatment, the lithium salt solution iscollected and processed into lithium carbonate, lithium hydroxide, orlithium phosphate.

In some embodiments, the uncoated ion exchange particles of the porousbead are comprised of an ion exchange material wherein the ion exchangematerial comprises Li₄Mn₅O₁₂, Li_(1.6)Mn_(1.6)O₄, Li₂MO₃ (M=Ti, Mn, Sn),LiFePO₄, solid solutions thereof, or combinations thereof. The uncoatedion exchange particles of the porous bead has an average diameter lessthan about 10 nm, less than about 20 nm, less than about 30 nm, lessthan about 40 nm, less than about 50 nm, less than about 60 nm, lessthan about 70 nm, less than about 80 nm, less than about 90 nm, lessthan about 100 nm, less than about 1,000 nm, less than about 10,000 nm,less than about 100,000 nm, more than about 10 nm, more than about 20nm, more than about 30 nm, more than about 40 nm, more than about 50 nm,more than about 60 nm, more than about 70 nm, more than about 80 nm,more than about 90 nm, more than about 100 nm, more than about 1,000 nm,more than about 10,000 nm, from about 1 nm to about 10,000 nm, fromabout 1 nm to about 1,000 nm, from about 1 nm to about 100 nm, fromabout 1 nm to about 80 nm, from about 1 nm to about 60 nm, from about 1nm to about 40 nm, or from about 1 nm to about 20 nm. The uncoated ionexchange particles of the porous bead are created by synthesizing theion exchange material using a method such as hydrothermal, solid state,microwave, or combinations thereof. The uncoated ion exchange particlesof the porous bead is treated with an acid solution prepared withhydrochloric acid, sulfuric acid, nitric acid, or combinations thereofwherein the concentration of the acid solution is greater than about 0.1M, greater than about 0.5 M, greater than about 2 M, greater than about5 M, or combinations thereof. During acid treatment, the uncoated ionexchange particles of the porous bead absorb hydrogen ions whilereleasing lithium ions. The ion exchange material is converted to aprotonated state. After treatment in acid, the protonated uncoated ionexchange particles are treated with a liquid resource wherein the liquidresource is a natural brine, a dissolved salt flat, a concentratedbrine, a processed brine, a synthetic brine, an oilfield brine, liquidfrom an ion exchange process, liquid from a solvent extraction process,leachate from minerals, leachate from clays, leachate from recycledproducts, leachate from recycled materials, or combinations thereof. Theuncoated ion exchange particles absorb lithium ions while releasinghydrogen ions. After acid treatment, the lithium salt solution iscollected and processed into lithium carbonate, lithium hydroxide, orlithium phosphate.

In some embodiments, there is a combination of coated ion exchangeparticles and uncoated ion exchange particles in the porous bead. Thecombination of coated ion exchange particles and uncoated ion exchangeparticles in the porous bead is treated with an acid solution preparedwith hydrochloric acid, sulfuric acid, nitric acid, or combinationsthereof wherein the concentration of the acid solution is greater thanabout 0.1 M, greater than about 0.5 M, greater than about 2 M, greaterthan about 5 M, or combinations thereof. During acid treatment, thecombination of coated ion exchange particles and uncoated ion exchangeparticles in the porous bead absorb hydrogen ions while releasinglithium ions. The ion exchange material is converted to a protonatedstate. After treatment in acid, the combination of protonated coated ionexchange particles and protonated uncoated ion exchange particles in theporous bead are treated with a liquid resource wherein the liquidresource is a natural brine, a dissolved salt flat, a concentratedbrine, a processed brine, a synthetic brine, an oilfield brine, liquidfrom an ion exchange process, liquid from a solvent extraction process,leachate from minerals, leachate from clays, leachate from recycledproducts, leachate from recycled materials, or combinations thereof. Thecombination of protonated coated ion exchange particles and protonateduncoated ion exchange particles in the porous bead absorb lithium ionswhile releasing hydrogen ions. After acid treatment, the lithium saltsolution is collected and processed into lithium carbonate, lithiumhydroxide, or lithium phosphate.

Methods Using Coated Ion Exchange Particles, Porous Structure, and/orPorous Beads in a Column

In an aspect described herein are methods of extracting lithium from aliquid resource, wherein the methods using coated ion exchangeparticles, porous structures, and/or porous beads is conducted in acolumn. The coated ion exchange particles are as hereinbefore described.The porous structures are as hereinbefore described. The porous beadsare as hereinbefore described.

The coated ion exchange particles, porous structures, and/or porousbeads are loaded into an ion exchange column. One example of an ionexchange column is shown in FIG. 3. The ion exchange column directsliquids to percolate around the coated ion exchange particles, porousstructures, and/or porous beads, thereby facilitating ion exchangebetween the coated ion exchange particles, the uncoated ion exchangeparticles, and/or combinations thereof, and the liquid resource.

When the coated ion exchange particles, porous structures, and/or porousbeads are used in an ion exchange column, the liquid resource containinglithium ions is pumped through the ion exchange column so that thecoated ion exchange particles, the uncoated ion exchange particles,and/or combinations thereof absorb lithium from the liquid resourcewhile releasing hydrogen. After the particles have absorbed lithium, anacid solution is pumped through the column so that the coated ionexchange particles, the uncoated ion exchange particles, and/orcombinations thereof release lithium ions into the acid solution whileabsorbing hydrogen ions.

The column is optionally operated in co-flow mode with the liquidresource and acid solution alternately flowing through the column in thesame direction or the column is optionally operated in counter-flow modewith a liquid resource and acid solution alternately flowing through thecolumn in opposite directions. Between flows of the liquid resource andthe acid solution, the column is optionally treated or washed with wateror other solutions for purposes such as adjusting pH in the column orremoving potential contaminants. Before or after the liquid resourceflows through the column, the pH of the liquid is optionally adjustedwith NaOH or other chemicals to facilitate the ion exchange reaction aswell as handling or disposal of the spent liquid resource. Before orafter the liquid resource flows through the column, the liquid resourceis optionally subjected to other processes including other ion exchangeprocesses, solvent extraction, evaporation, chemical treatment, orprecipitation to remove lithium ions, to remove other chemical species,or to otherwise treat the brine. When the ion exchange particles aretreated with acid, a lithium ion solution is produced. This lithium ionsolution is further processed to produce lithium chemicals. In someembodiments, these lithium chemicals are supplied for an industrialapplication.

In some embodiments, lithium ions are extracted from a liquid resource.The liquid resource is a natural brine, a dissolved salt flat, aconcentrated brine, a processed brine, a synthetic brine, an oilfieldbrine, liquid from an ion exchange process, liquid from a solventextraction process, leachate from minerals, leachate from clays,leachate from recycled products, leachate from recycled materials, orcombinations thereof.

Lithium Ion Salt Solutions

In an aspect described herein are lithium salt solutions with animpurity concentration of about 1 ppb to about 10 ppm wherein theimpurity concentration denotes the presence of coated ion exchangeparticles during the production of the lithium salt solution. In someembodiments, the impurity is present in a concentration of more than 1ppb, more than 5 ppb, more than 10 ppb, more than 100 ppb, more than 1ppm, more than 2 ppm, more than 3 ppm, more than 4 ppm, more than 5 ppm,more than 6 ppm, more than 7 ppm, more than 8 ppm, more than 9 ppm, lessthan 10 ppm, less than 9 ppm, less than 8 ppm, less than 7 ppm, lessthan 6 ppm, less than 5 ppm, less than 4 ppm, less than 3 ppm, less than2 ppm, less than 1 ppm, less than 100 ppb, less than 10 ppb, less than 5ppb, from about 1 ppb to about 10 ppm, from about 5 ppb to about 10 ppm,from about 10 ppb to about 10 ppm, from about 50 ppb to about 10 ppm,from about 100 ppb to about 10 ppm, from about 1 ppm to about 10 ppm,from about 2 ppm to about 10 ppm, from about 4 ppm to about 10 ppm, fromabout 6 ppm to about ppm, or from about 8 ppm to about 10 ppm. Whenlithium ions are eluted from the coated ion exchange particles using anacid solution, some small amount of the coating material are dissolved.These dissolved elements will be released with the lithium. In someembodiments, the lithium is purified, but some very small concentrationof elements from the coating material remain within the lithium productas an impurity. In some embodiments this impurity concentration is onthe order of parts-per-billion, and is detected using InductivelyCoupled Plasma-Atomic Emission Spectroscopy (ICP-AES) or InductivelyCoupled Plasma-Mass Spectrometry (ICP-MS). In one embodiment, ICP-AES isused to measure impurity concentrations of Zr ions or Ti ions from ZrO₂or TiO₂ coatings at wavelengths of 343.823 nm or 336.121 nm.

In some embodiments, the concentrated lithium ion solution is furtherprocessed into lithium raw materials using methods such as solventextraction, ion exchange, chemical substitution, chemical precipitation,electrodialysis, electrowinning, evaporation, heat treatment, orcombinations thereof. In some embodiments, the concentrated lithium ionsolution is further processed into lithium chemicals such as lithiumchloride, lithium carbonate, lithium hydroxide, lithium phosphate,lithium metal, lithium metal oxide, lithium metal phosphate, lithiumsulfide, or combinations thereof.

In some embodiments, the lithium chemicals produced is used in anindustrial application such as lithium batteries, metal alloys, glass,grease, or combinations thereof. In some embodiments, the lithiumchemicals produced are used in an application such as lithium batteries,lithium-ion batteries, lithium sulfur batteries, lithium solid-statebatteries, and combinations thereof.

EXAMPLES Example 1 Synthesis of Coated Ion Exchange Particles(Li₄Mn₅O₁₂/ZrO₂)

The coated ion exchange particles are comprised of an ion exchangematerial and a coating material. The ion exchange material is Li₄Mn₅O₁₂and the coating material is ZrO₂. The particles are created by firstsynthesizing Li₄Mn₅O₁₂ and then depositing the coating on the surface ofthe Li₄Mn₅O₁₂.

The ion exchange material, Li₄Mn₅O₁₂ is synthesized using hydrothermalsynthesis, solid state synthesis, microwave synthesis or combinationsthereof. The coating material (ZrO₂) is deposited on the surface of theLi₄Mn₅O₁₂ using chemical vapor deposition, hydrothermal deposition,solvothermal deposition, sol-gel deposition, precipitation, microwavedeposition or by suspending Li₄Mn₅O₁₂ in a solvent and then addingreagents including metal chloride, metal oxychloride, metal alkoxide,water, acid, base, or combinations thereof. The particles comprise of 98wt. % ion exchange material (Li₄Mn₅O₁₂) and 2 wt. % of the coating(ZrO₂). The particles have a mean diameter of 1 microns, and the coatingthickness is approximately 2 nm.

Example 2 Synthesis of Coated Ion Exchange Particles (Li₄Mn₅O₁₂/ZrO₂)

The coated ion exchange particles were comprised of an ion exchangematerial and a coating material. The ion exchange material was Li₄Mn₅O₁₂and the coating material was ZrO₂. The particles were created by firstsynthesizing Li₄Mn₅O₁₂ and then depositing the coating on the surface ofthe Li₄Mn₅O₁₂.

The Li₄Mn₅O₁₂ ion exchange material was synthesized using a solid-statemethod from electrolytic manganese dioxide and lithium nitrateprecursors. The precursors were ball-milled using 5 mm ZrO₂ grindingmedia for 30 minutes in a planetary ball mill. The resulting mixture wasfired in a furnace with a heating rate of 5° C./min up to 550° C. for 36hours and then cooled slowly to room temperature. The resulting powderwas comprised of Li₄Mn₅O₁₂ ion exchange material. A ZrO₂ coating wasdeposited on the Li₄Mn₅O₁₂ ion exchange material. The ion exchangematerial was suspended in a mixture of butanol, ethanol, and water withvigorous stirring, and a mixture of butanol and zirconium butoxide wasdripped into the suspension over the course of 30 minutes. Thesuspension was stirred for 2 hours to allow the zirconium butoxide toreact with the water and form a ZrO₂ precursor on the particle surfaces.The coated powder was then fired in a furnace at 400° C. for 2 hours.The resulting powder was coated ion exchange particles comprised ofLi₄Mn₅O₁₂ particles with ZrO₂ coatings. The particles were comprised of98 wt. % ion exchange material (Li₄Mn₅O₁₂) and 2 wt. % of the coating(ZrO₂). The particles had a mean diameter of 1 micron, and the coatingthickness was approximately 2 nm.

Example 3 Synthesis of Coated Ion Exchange Particles (Li₂TiO₃/SiO₂)

The coated ion exchange particles were comprised of an ion exchangematerial and a coating material. The ion exchange material was Li₂TiO₃and the coating material was SiO₂. The particles were created by firstsynthesizing Li₂TiO₃ and then depositing the SiO₂ coating on the surfaceof the Li₂TiO₃.

The Li₂TiO₃ powder was synthesized using a solid-state method fromtitanium dioxide and lithium carbonate precursors. The precursors wereball-milled using 5 mm ZrO₂ grinding media for 30 minutes in a planetaryball mill. The resulting mixture was fired in a furnace with a heatingrate of 5° C./min up to 700° C. for 24 hours and then cooled slowly toroom temperature. The resulting powder was comprised of Li₂TiO₃ ionexchange material. A SiO₂ coating was deposited on the Li₂TiO₃ ionexchange material. The ion exchange material was suspended in a mixtureof ethanol and water with vigorous stirring, and a mixture of tetraethylorthosilicate (TEOS), water, and hydrochloric acid was dripped into thesuspension over the course of 120 minutes. The suspension was stirredfor 2 hours to allow the TEOS to deposit on the particle surfaces, andthe solvent was evaporated. The coated powder was then fired in afurnace at 400° C. for 2 hours. The resulting powder was coated ionexchange particles comprised of Li₂TiO₃ particles with SiO₂ coatings.The particles were comprised of 96 wt. % ion exchange material and 4 wt.% of the coating. The particles had a mean diameter of 4 microns, andthe coating thickness was approximately 35 nm.

Example 4 Use of Coated Ion Exchange Particles (Li₄Mn₅O₁₂/ZrO₂)

Lithium is extracted from a brine using coated ion exchange particles(Li₄Mn₅O₁₂/ZrO₂). The brine is an aqueous solution containing 50,000 ppmNa and 1,000 ppm Li. The coated ion exchange particles are treated withHCl acid to yield LiCl in solution. During acid treatment, the coatedion exchange particles absorb hydrogen ions while releasing lithiumions. The Li₄Mn₅O₁₂ active material is converted to a protonated state.The ZrO₂ coating allows diffusion of hydrogen and lithium respectivelyto and from the active material while providing a protective barrierthat limits dissolution of manganese and oxygen from the activematerial. The solution is collected for elemental analysis to measurelithium yield.

After treatment in acid, the protonated coated ion exchange particlesare treated with brine wherein the coated ion exchange particles absorblithium ions while releasing hydrogen ions. The coated ion exchangeparticles are converted from a protonated state to a lithiated state.The solution is collected for elemental analysis to measure lithiumuptake.

The lithiated coated ion exchange particles are then treated again withacid to yield lithium ions in solution. The cycle of protonation andlithiation is repeated to extract lithium ions from the brine and yielda LiCl solution. Dissolution and degradation of the active material inacid is limited due to the coating providing a protective barrier.Dissolution of the active material is measured through elementalanalysis of the acid solution following stirring.

Example 5 Use of Coated Ion Exchange Particles (Li₂TiO₃/SiO₂)

Lithium was extracted from a brine using coated ion exchange particles(Li₂TiO₃/SiO₂). The brine was an aqueous solution containing 50,000 ppmNa, 30,000 ppm Ca, 5,000 ppm Mg, and 100 ppm Li. The coated ion exchangeparticles were treated with HCl acid to yield LiCl in solution. Duringacid treatment, the coated ion exchange particles absorbed hydrogen ionswhile releasing lithium ions. The Li₂TiO₃ active material was convertedto a protonated state. The SiO₂ coating allowed diffusion of hydrogenions and lithium ions respectively to and from the active material whileproviding a protective barrier that limited dissolution of titanium andoxygen from the active material. The solution was collected forelemental analysis to measure lithium yield. FIG. 4. depicts the effectof the coating, which limits dissolution of the material while allowinglithium release.

After treatment in acid, the protonated coated ion exchange particleswere treated with brine wherein the coated ion exchange particlesabsorbed lithium ions while releasing hydrogen ions. The particles wereconverted from a protonated state to a lithiated state. The solution wasthen collected for elemental analysis to measure lithium uptake.

The lithiated coated ion exchange particles were then treated again withacid to yield lithium in solution. The cycle of protonation andlithiation was repeated to extract lithium ions from the brine and yielda LiCl solution. Dissolution and degradation of the active material inacid was limited due to the coating providing a protective barrier.Dissolution of the active material was measured through elementalanalysis of the acid solution following stirring.

Example 6 Use of Porous Beads Containing Coated Ion Exchange Particles(Li₄Mn₅O₁₂/ZrO₂)

Lithium is extracted from a brine using porous beads. The porous beadsare comprised of coated ion exchange particles (Li₄Mn₅O₁₂/ZrO₂) and apolymer matrix. The coated ion exchange particles are comprised of aLi₄Mn₅O₁₂ with a ZrO₂ coating. The ion exchange particles contain 95 wt% Li₄Mn₅O₁₂ and 5 wt % ZrO₂. The particles are approximately sphericalwith a mean diameter of 2 microns, and the coating thickness isapproximately 12 nm. The polymer matrix is comprised of polyvinylidenefluoride. The porous beads are created by dissolving polyvinylidenefluoride in N-methyl-2-pyrrolidone (NMP) to form a solution. Thissolution is then mixed with the coated ion exchange particles to form aslurry. The slurry is dripped into an aqueous solution to form beads.The porous beads are comprised of 10 wt. % polyvinylidene fluoridematrix and 90 wt. % coated ion exchange particles. The porous beads havean average diameter of 2 mm and a porosity of 35%.

The porous beads contain pores with a distribution of pore sizesproviding diffusion channels from the bead surface into the beadinterior and to the ion exchange particles. When the porous beads aresubmerged in aqueous or other solutions, the pores are infiltrated withthe solutions. The beads have a distribution of shapes that areapproximately spherical on average with a 1 mm average diameter.

The brine is an aqueous chloride solution containing 100 ppm Li, 40,000ppm Na, 30,000 ppm Ca, and 3,000 ppm Mg. The porous beads are treatedwith HCl acid to yield LiCl in solution. 1 g of the beads are stirred in30 mL of 1 M HCl acid for 4 hours at room temperature. The pores in thebeads allow the acid solution to penetrate into the bead and access theion exchange particles. Therefore, the ion exchange particles absorbhydrogen ions from the acid while releasing lithium ions into the acid.The Li₄Mn₅O₁₂ of the coated ion exchange particles in the porous beadsis converted to a protonated state Li_(4-x)H_(x)Mn₅O₁₂ where x may beabout to 3.5. The ZrO₂ coating of the coated ion exchange particlesallows diffusion of hydrogen ions and lithium ions respectively to andfrom the ion exchange material while providing a protective barrier thatlimits dissolution of manganese and oxygen from the ion exchangematerial. After 4 hours of stirring, the solution is collected forelemental analysis to measure lithium yield.

After treatment in acid, the protonated porous beads are treated withbrine wherein the coated ion exchange particles absorb lithium ionswhile releasing hydrogen ions. The protonated porous beads are stirredin 500 mL of brine for 4 hours at room temperature. The pores in theporous beads allow the brine solution to penetrate into the porous beadand access the coated ion exchange particles. Therefore, the coated ionexchange particles absorb lithium ions from the brine while releasinghydrogen ions into the brine. The coated ion exchange particles in theporous beads are converted from a protonated state to a lithiated stateLi_(4-x)H_(x)Mn₅O₁₂ where x may be about to 2. After 4 hours ofstirring, the solution is collected for elemental analysis to measurelithium uptake.

The lithiated porous beads are then treated again with acid to yieldlithium ions in. The cycle of protonation and lithiation is repeated toextract lithium ions from the brine and yield a LiCl solution. The poresin the porous beads facilitate penetration of the acid and brinesolutions into the porous beads, facilitating absorption and release oflithium ions and hydrogen ions by the coated ion exchange particles(Li₄Mn₅O₁₂/ZrO₂) in the porous bead. Dissolution and degradation of theactive material in acid is limited due to the ZrO₂ coating providing aprotective barrier. Dissolution of the active material is measured withelemental analysis of the acid solution following stirring.

Example 7 Use of Porous Beads Containing Coated Ion Exchange Particles(Li₄Mn₅O₁₂/ZrO₂) in a Column

Lithium is extracted from a brine using an ion exchange column loadedwith porous beads containing coated ion exchange particles(Li₄Mn₅O₁₂/ZrO₂).

The coated ion exchange particles are comprised of an active materialand a protective surface coating. The active material is Li₄Mn₅O₁₂ andthe coating is ZrO₂. The particles are created by synthesizing Li₄Mn₅O₁₂and then depositing the coating on the surface of the Li₄Mn₅O₁₂. Thecoated ion exchange particles are comprised of 95 wt. % active materialconstitutes and 5 wt. % of the coating and have a mean diameter of 2microns, and a coating thickness is approximately 12 nm.

The porous beads are created by dissolving polyvinylidene fluoride inN-methyl-2-pyrrolidone (NMP) to form a solution. This solution is thenmixed with the coated ion exchange particles to form a slurry. Theslurry is dripped into an aqueous solution to form beads. The porousbeads are comprised of 10 wt. % polyvinylidene fluoride matrix and 90wt. % coated ion exchange particles. The porous beads have an averagediameter of 2 mm and a porosity of 35%.

The brine is natural brine containing approximately 500 ppm Li, 50,000ppm Na, and other chemical species including K, Mg, Ca, and sulfate.

The ion exchange column is 2 meters in length and 50 cm in diameter. Thecolumn is loaded with the porous beads. 10 M HCl is pumped into thebottom of the column to elute a LiCl solution out the top of the column.The coated ion exchange particles absorb hydrogen ions while releasinglithium ions to yield LiCl. The Li₄Mn₅O₁₂ active material is convertedto a protonated state. Lithium recovery from the column is monitoredusing pH measurements and elemental analysis. After lithium recovery,the column is flushed with water.

After acid treatment, brine is pumped down through the column. Thecoated ion exchange particles absorb lithium ions while releasinghydrogen ions. The protonated material is converted to a lithiatedstate. Lithium ion uptake by the porous beads in the column is monitoredusing pH measurements and elemental analysis. The brine exiting thecolumn is adjusted to a neutral pH using NaOH. After lithium ion uptake,the column is flushed with water.

The column is operated by repeating the previously described steps ofacid and brine pumping in alternation. This column operates to extractlithium from the brine and produce a concentrated LiCl solution. Duringcolumn operation, the coated ion exchange particles are protected fromdissolution and degradation due to the surface coating, which provides aprotective barrier.

The LiCl solution from the column operation is processed into lithiumraw materials including Li₂CO₃, LiOH, and Li metal. These lithium rawmaterials are sold for use in batteries, alloys, and other products.

Example 8 Use of Porous Beads Containing Coated Ion Exchange Particles(Li₂TiO₃/SiO₂) in a Column

Lithium is extracted from a brine using an ion exchange column loadedwith porous beads containing coated ion exchange particles.

The coated ion exchange particles (Li₂TiO₃/SiO₂) are comprised of anactive material and a protective surface coating. The active material isLi₂TiO₃ and the coating is SiO₂. The particles are created bysynthesizing Li₂TiO₃ and then depositing the SiO₂ coating on the surfaceof the Li₂TiO₃. The coated ion exchange particles are comprised of 96wt. % active material and 4 wt. % of the coating and have a meandiameter of 4 microns, and the coating thickness is approximately 35 nm.

The porous beads are created by dissolving polyvinylchloride inN-methyl-2-pyrrolidone (NMP) to form a solution. This solution is thenmixed with the coated ion exchange particles to form a slurry. Theslurry is dripped into an aqueous solution to form porous beads. Thebeads are comprised of 20 wt. % polyvinyl chloride matrix and 80 wt. %coated ion exchange particles. The beads have an average diameter of 1mm and a porosity of 25%.

The brine is a natural brine containing approximately 50 ppm Li, 60,000ppm Na, and other chemical species including K, Mg, Ca, and Cl.

The ion exchange column is 2 meters in length and 50 cm in diameter. Thecolumn is loaded with the beads. 0.5 M HCl is pumped into the bottom ofthe column to elute a LiCl solution out the top of the column. Thecoated ion exchange particles absorb hydrogen ions while releasinglithium ions to yield LiCl. The Li₂TiO₃ active material is converted toa protonated state. Lithium recovery from the column is monitored usingpH measurements and elemental analysis. After lithium recovery, thecolumn is flushed with water.

After acid treatment, brine is pumped down through the column. Thecoated ion exchange particles (Li₂TiO₃/SiO₂) absorb lithium ions whilereleasing hydrogen ions. The protonated material is converted to alithiated state. Lithium ion uptake by the porous beads in the column ismonitored using pH measurements and elemental analysis. The brineexiting the column is adjusted to a neutral pH using NaOH. After lithiumuptake, the column was flushed with an aqueous solution to removecontaminants.

The column is operated by repeating the previously described steps ofacid and brine pumping in alternation. This column is operated toextract lithium from the brine and produce a concentrated LiCl solution.During column operation, the ion exchange particles are protected fromdissolution and degradation due to the surface coating, which provides aprotective barrier.

The LiCl solution from the column operation is processed into lithiumraw materials including Li₂CO₃, LiOH, and Li metal. These lithium rawmaterials are sold for use in batteries, alloys, and other products.

While preferred embodiments of the present invention have been shown anddescribed herein, it will be obvious to those skilled in the art thatsuch embodiments are provided by way of example only. Numerousvariations, changes, and substitutions will now occur to those skilledin the art without departing from the invention. It should be understoodthat various alternatives to the embodiments of the invention describedherein may be employed in practicing the invention. It is intended thatthe following claims define the scope of the invention and that methodsand structures within the scope of these claims and their equivalents becovered thereby.

What is claimed is:
 1. A method of extracting lithium from a liquidresource, comprising: (a) contacting a coated ion exchange particlecomprising an ion exchange material and a coating material, with aliquid resource to produce lithiated coated ion exchange particles; and(b) treating the lithiated coated ion exchange particles with an acidsolution to produce a salt solution comprising lithium ions, wherein theion exchange material is selected from the group consisting ofLi₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃, Li₂MnO₃, Li₂SnO₃, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiAlO₂, LiCuO₂, LiTiO₂, Li₄TiO₄, Li₇Ti₁₁O₂₄, Li₃VO₄,Li₂Si₃O₇, LiFePO₄, LiMnPO₄, Li₂CuP₂O₇, Al(OH)₃, LiCl.xAl(OH)₃.yH₂O,SnO₂.xSb₂O₅.yH₂O, TiO₂.xSb₂O₅.yH₂O, solid solutions thereof, andcombinations thereof; wherein x is from 0.1-10; and y is from 0.1-10;and wherein the coating material comprises TiO₂, ZrO₂, MoO₂, SnO₂,Nb₂O₅, Ta₂O₅, Li₂TiO₃, SiO₂, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, LiTaO₃, AlPO₄,LaPO₄, ZrSiO₄ , ZrP₂O₇, MoP₂O₇, Mo₂P₃O₁₂, BaSO₄, AlF₃, SiC, TiC, ZrC,Si₃N₄, ZrN, BN, carbon, graphitic carbon, amorphous carbon, solidsolutions thereof, or a combination thereof.
 2. The method of claim 1,wherein the salt solution further comprises an impurity derived from thecoated ion exchange particle.
 3. The method of claim 2, wherein theimpurity is present in a concentration of about 1 ppb to about 10 ppm.4. The method of claim 1, wherein the liquid resource is a naturalbrine, a dissolved salt flat, seawater, concentrated seawater, adesalination effluent, a concentrated brine, a processed brine, anoilfield brine, a liquid from an ion exchange process, a liquid from asolvent extraction process, a synthetic brine, a leachate from an ore orcombination of ores, a leachate from a mineral or combination ofminerals, a leachate from a clay or combination of clays, a leachatefrom recycled products, a leachate from recycled materials, orcombinations thereof.
 5. The method of claim 1, wherein the acidsolution comprises hydrochloric acid, sulfuric acid, phosphoric acid,hydrobromic acid, chloric acid, perchloric acid, nitric acid, formicacid, acetic acid, or combinations thereof.
 6. The method of claim 1,wherein the coating material limits dissolution of the ion exchangematerial.
 7. The method of claim 1, wherein the coating material allowsdiffusion of lithium ions and hydrogen ions to and from the ion exchangematerial.
 8. The method of claim 1, wherein the ion exchange material isselected from the group consisting of Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃,Li₂MnO₃, Li₂SnO₃, LiMn₂O₄, Li_(1.6)Mn_(1.6)O₄, LiTiO₂, Li₄TiO₄,Li₇Ti₁₁O₂₄, LiFePO₄, and LiMnPO₄.
 9. The method of claim 1, wherein theion exchange material is selected from the group consisting ofLi₄Mn₅O₁₂, Li₂MnO₃, LiMn₂O₄, Li_(1.6)Mn_(1.6)O₄, and LiMnPO₄.
 10. Themethod of claim 1, wherein the ion exchange material is selected fromthe group consisting of Li₄Ti₅O₁₂, Li₂TiO₃, LiTiO₂, Li₄TiO₄, andLi₇Ti₁₁O₂₄.
 11. The method of claim 1, wherein the ion exchange materialis selected from the group consisting of Li₂SnO₃ and LiFePO₄.
 12. Themethod of claim 1, wherein the coating material comprises TiO₂, ZrO₂,MoO₂, Li₂TiO₃, SiO₂, Li₂ZrO₃, Li₂MoO₃, LiNbO₃, ZrSiO₄, AlF₃, SiC, Si₃N₄,graphitic carbon, amorphous carbon, solid solutions thereof, or acombination thereof.
 13. The method of claim 1, wherein the coatingmaterial comprises TiO₂, ZrO₂, or SiO₂.
 14. The method of claim 1,wherein the ion exchange material is selected from the group consistingof Li₄Mn₅O₁₂, Li₄Ti₅O₁₂, Li₂TiO₃, Li₂MnO₃, Li₂SnO₃, LiMn₂O₄,Li_(1.6)Mn_(1.6)O₄, LiTiO₂, Li₄TiO₄, Li₇Ti₁₁O₂₄, LiFePO₄, and LiMnPO₄,and the coating material comprises TiO₂, ZrO₂, or SiO₂.
 15. The methodof claim 1, wherein the ion exchange material is selected from the groupconsisting of Li₄Mn₅O₁₂, Li₂MnO₃, LiMn₂O₄, Li_(1.6)Mn_(1.6)O₄, andLiMnPO₄, and the coating material comprises TiO₂, ZrO₂, or SiO₂.
 16. Themethod of claim 1, wherein the ion exchange material is selected fromthe group consisting of Li₄Ti₅O₁₂, Li₂TiO₃, LiTiO₂, Li₄TiO₄, andLi₇Ti₁₁O₂₄, and the coating material comprises TiO₂, ZrO₂, or SiO₂. 17.The method of claim 1, wherein the ion exchange material is selectedfrom the group consisting of Li₂SnO₃ and LiFePO₄, and the coatingmaterial comprises TiO₂, ZrO₂, or SiO₂.
 18. The method of claim 1,wherein the coated ion exchange particle has an average diameter fromabout 20 μm to about 200 μm.
 19. The method of claim 1, wherein thecoated ion exchange particle has an average diameter of less than 100μm.
 20. The method of claim 1, wherein the coated ion exchange particlehas an average diameter of less than 60 μm.
 21. The method of claim 1,wherein the coated ion exchange particle has an average diameter of lessthan 30 μm.
 22. The method of claim 1, wherein the coated ion exchangeparticle has an average diameter of less than 20 μm.